JPH11253942A - Immersion type mobile membrane separation wastewater treatment apparatus - Google Patents

Immersion type mobile membrane separation wastewater treatment apparatus

Info

Publication number
JPH11253942A
JPH11253942A JP6023298A JP6023298A JPH11253942A JP H11253942 A JPH11253942 A JP H11253942A JP 6023298 A JP6023298 A JP 6023298A JP 6023298 A JP6023298 A JP 6023298A JP H11253942 A JPH11253942 A JP H11253942A
Authority
JP
Japan
Prior art keywords
membrane
tank
reaction
immersed
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.)
Granted
Application number
JP6023298A
Other languages
Japanese (ja)
Other versions
JP3506603B2 (en
Inventor
Masaharu Nurishi
雅治 塗師
Seiji Izumi
清司 和泉
Kenji Kubota
謙治 久保田
Yutaka Yamada
山田  豊
Kazuhiko Kariya
一彦 刈谷
Susumu Kawakami
進 川上
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 JP06023298A priority Critical patent/JP3506603B2/en
Publication of JPH11253942A publication Critical patent/JPH11253942A/en
Application granted granted Critical
Publication of JP3506603B2 publication Critical patent/JP3506603B2/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

  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a noise-controlled immersion type mobile membrane separation wastewater treatment apparatus which can be transported as an integrated unit of the entire apparatus. SOLUTION: A reaction area 4 and a discharge area 5, which are separated by an partition wall 3, are formed in a tank body 2 in the form of a transportable unit, a membrane separator 7 in which a casing 8 is integrated with the tank body is immersed in the reaction area receiving raw water, plane membrane type membrane cartidges 9 are arranged in parallel in the vertical direction in the casing 8, a filtrate discharge system 12 in which the base end side communicates with the membrane filtrate channel of the membrane cartridge and the tip side communicates with the discharge area is installed, an air diffuser 11 is arranged below the membrane cartridge in the membrane separator 7, and an underwater blower 17 for supplying aeration air to the air diffuser 11 is immersed in the tank.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、下水・廃水に対す
る小規模な水処理設備に係り、移動式浸漬型膜分離汚水
処理装置に関する。
The present invention relates to a small-scale water treatment facility for sewage and wastewater, and more particularly to a mobile immersion type membrane separation sewage treatment apparatus.

【0002】[0002]

【従来の技術】従来、下水・廃水等の被処理水を生物学
的処理する形態としては、例えば図6に示すものがあ
り、流入する被処理水41を曝気槽42へ受け入れると
ともに、曝気槽42において散気装置43から空気を供
給しながら連続的に被処理水を生物学的処理し、曝気槽
42の混合液44を沈殿槽45で固液分離し、沈殿槽4
5における上澄水46を放流槽47を経て系外へ放流
し、沈殿槽45で沈降分離した汚泥を曝気槽42へ返送
することにより、活性汚泥の系外への流出を抑制すると
ともに、曝気槽42における汚泥濃度を高めていた。
2. Description of the Related Art Conventionally, as an example of biological treatment of sewage, wastewater or other treated water, there is a form shown in FIG. 6, in which incoming treated water 41 is received in an aeration tank 42, At 42, the water to be treated is continuously subjected to biological treatment while air is supplied from an air diffuser 43, and a mixed solution 44 in an aeration tank 42 is solid-liquid separated in a sedimentation tank 45.
5 is discharged out of the system through a discharge tank 47, and the sludge settled and separated in the settling tank 45 is returned to the aeration tank 42, thereby suppressing the outflow of the activated sludge to the outside of the system. 42 had increased the sludge concentration.

【0003】[0003]

【発明が解決しようとする課題】ところで、イベント会
場や建設現場においては、仮設トイレを設置して人々の
使用に供しているが、イベント会場や建設現場の規模が
大きくなると、使用人数および使用頻度が多数となり、
仮設トイレで対応することは、その設置数に限りがある
ことから困難であり、汚物の回収が遅れると不衛生な状
況が現出する。このために、大規模なイベント会場や建
設現場においては、小規模の水処理設備を設置し、その
対応を行なっている。
In the event venues and construction sites, temporary toilets are installed for use by people. However, as the size of the event venues and construction sites increases, the number of employees and the frequency of use will increase. Becomes large,
It is difficult to deal with temporary toilets due to the limited number of installations, and if the collection of waste is delayed, unsanitary situations will appear. For this reason, small-scale water treatment facilities are installed at large event venues and construction sites to respond to them.

【0004】しかし、上記したように、活性汚泥の分離
を沈殿槽45で重力沈降により行う場合には、その分離
効率が低いために、曝気槽42における微生物濃度を高
濃度に維持することが困難で、曝気槽42における被処
理水41の滞留時間を長く必要とし、曝気槽42の槽容
量が大きくなるとともに、沈殿槽45においても沈降速
度に見合う槽内滞留時間を必要とし、沈殿槽45の槽容
量が大きくなる。
However, as described above, when the activated sludge is separated by gravity sedimentation in the sedimentation tank 45, it is difficult to maintain the microorganism concentration in the aeration tank 42 at a high concentration due to the low separation efficiency. Therefore, the residence time of the water 41 to be treated in the aeration tank 42 is required to be long, and the tank capacity of the aeration tank 42 is increased. The tank capacity increases.

【0005】このために、曝気槽と沈殿槽とを搬送可能
な一体式のユニットとして構成することはできず、イベ
ント会場や建設現場に設置する場合には、設備を複数に
分割して搬入して後に、現地において組み立てる必要が
あり、繊維強化プラスチック(FRP)やコンクリート
(RC)により製作している。また、短期間の使用を目
的とする水処理設備においては、ポンプやブロワなどの
付帯設備を配置する機械室等の上屋を省く場合が多く、
ポンプやブロワ等から発生する騒音対策が課題であっ
た。
[0005] For this reason, the aeration tank and the sedimentation tank cannot be configured as an integral unit that can be transported, and when installed at an event site or a construction site, the equipment is divided into a plurality of units and carried in. Later, it is necessary to assemble it locally, and it is made of fiber reinforced plastic (FRP) or concrete (RC). In addition, water treatment facilities intended for short-term use often omit sheds such as machine rooms where auxiliary equipment such as pumps and blowers are arranged,
Noise countermeasures such as those generated by pumps and blowers have been an issue.

【0006】本発明は上記した課題を解決するものであ
り、装置全体を一体的なユニットとして搬送することが
でき、かつ騒音の少ない移動式浸漬型膜分離汚水処理装
置を提供することを目的とする。
An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide a mobile immersion type membrane separation sewage treatment apparatus which can transport the entire apparatus as an integrated unit and has low noise. I do.

【0007】[0007]

【課題を解決するための手段】上記した課題を解決する
ために、請求項1に係る本発明の移動式浸漬型膜分離汚
水処理装置は、搬送可能なユニット形式をなす槽体の内
部に、仕切壁を隔てて反応領域と放流領域を区画形成
し、被処理水が流入する反応領域にケーシングが槽体と
一体をなす膜分離装置を浸漬し、ケーシング内に複数の
平膜型の膜カートリッジを鉛直方向に平行に配置し、基
端側が膜カートリッジに連通するとともに、先端側が放
流領域に連通する透過液導出系を設け、膜分離装置にお
ける膜カートリッジの下方に散気装置を配置するととも
に、散気装置へ曝気空気を供給する水中ブロワを槽内に
浸漬したものである。
In order to solve the above-mentioned problems, a mobile immersion type membrane separation sewage treatment apparatus according to the present invention according to the first aspect of the present invention comprises a unit body capable of being transported inside a tank. A reaction area and a discharge area are defined with a partition wall therebetween, and a membrane separation device in which a casing is integrated with a tank body is immersed in a reaction area into which water to be treated flows, and a plurality of flat membrane type membrane cartridges are placed in the casing. Are arranged in parallel in the vertical direction, the base end side communicates with the membrane cartridge, the distal end side is provided with a permeate outlet system communicating with the discharge area, and the air diffuser is arranged below the membrane cartridge in the membrane separation device, An underwater blower that supplies aerated air to the air diffuser is immersed in the tank.

【0008】請求項2に係る本発明の移動式浸漬型膜分
離汚水処理装置は、搬送可能なユニット形式をなす槽体
の内部に、仕切壁を隔てて第1反応領域と第2反応領域
と放流領域を区画形成し、被処理水が流入する第1反応
領域と第2反応領域との間に連通路を設け、第1反応領
域と第2反応領域の何れか一方の反応領域に、他方の反
応領域へ槽内液を供給する水中ポンプを浸漬し、第2反
応領域にケーシングが槽体と一体をなす膜分離装置を浸
漬し、ケーシング内に複数の平膜型の膜カートリッジを
鉛直方向に平行に配置し、基端側が膜カートリッジに連
通するとともに、先端側が放流領域に連通する透過液導
出系を設け、膜分離装置における膜カートリッジの下方
に散気装置を配置するとともに、散気装置へ曝気空気を
供給する水中ブロワを槽内に浸漬したものである。
According to a second aspect of the present invention, there is provided a mobile immersion type membrane separation sewage treatment apparatus according to the present invention, wherein a first reaction region and a second reaction region are separated from each other by a partition wall inside a tank unit having a transportable unit. A discharge region is defined, and a communication path is provided between the first reaction region and the second reaction region into which the water to be treated flows, and one of the first reaction region and the second reaction region is connected to the other reaction region. The submersible pump that supplies the liquid in the tank to the reaction area is immersed, the membrane separation device in which the casing is integrated with the tank body is immersed in the second reaction area, and a plurality of flat membrane type membrane cartridges are vertically inserted into the casing. Are arranged in parallel with each other, a permeate outlet system is provided in which the base end side communicates with the membrane cartridge and the distal end side communicates with the discharge region, and an air diffuser is arranged below the membrane cartridge in the membrane separator, and the air diffuser Submersible blower that supplies aerated air to The in which was immersed in the bath.

【0009】請求項3に係る本発明の移動式浸漬型膜分
離汚水処理装置は、膜透過液流路が先端側において放流
領域の水面下に開口するサイフォン管路をなすものであ
る。
According to a third aspect of the present invention, there is provided a mobile immersion type membrane separation sewage treatment apparatus according to the present invention, wherein the membrane permeate flow path forms a siphon pipe which is opened below the water surface in the discharge area on the tip side.

【0010】[0010]

【発明の実施の形態】以下、本発明の実施形態を図面に
基づいて説明する。図1から図4において、移動式浸漬
型膜分離汚水処理装置1は、槽体2が車両等に積載して
搬送可能な独立したユニット形式の形態をなしており、
槽体2の内部には、仕切壁3を隔てて反応領域4と放流
領域5とを区画形成している。
Embodiments of the present invention will be described below with reference to the drawings. 1 to 4, a mobile immersion type membrane separation sewage treatment apparatus 1 has an independent unit type in which a tank body 2 can be loaded and transported on a vehicle or the like,
Inside the tank body 2, a reaction region 4 and a discharge region 5 are formed with a partition wall 3 therebetween.

【0011】被処理水6が流入する反応領域4には膜分
離装置7を浸漬しており、膜分離装置7はケーシング8
が槽体2と一体をなし、ケーシング8の内部に複数の平
膜型の膜カートリッジ9を鉛直方向に平行に配置してい
る。ケーシング8は、上部域に膜カートリッジ9を収納
し、膜カートリッジ9を一定間隔に挿入配置するための
複数の案内溝10を相対向する内側面に有しており、下
部域に膜カートリッジ9の下方に配置した散気装置11
を収納し、下部域が曝気空気のガイドを兼ねている。
A membrane separation device 7 is immersed in the reaction area 4 into which the water 6 to be treated flows, and the membrane separation device 7 is
Is formed integrally with the tank body 2, and a plurality of flat membrane type membrane cartridges 9 are arranged inside the casing 8 in parallel in the vertical direction. The casing 8 accommodates the membrane cartridge 9 in an upper region, and has a plurality of guide grooves 10 on opposite inner surfaces for inserting and arranging the membrane cartridge 9 at regular intervals. Air diffuser 11 arranged below
The lower region also serves as a guide for aerated air.

【0012】膜分離装置7の各膜カートリッジ9は、剛
性を有する濾板の表面に有機濾過膜を配置した平膜型を
なし、濾板の膜透過液流路が透過液導出系12に連通し
ている。透過液導出系12は、濾板の膜透過液流路に連
通するフレキシブルなチューブ13と、チューブ13を
集合して連結する集液ヘッダー14と、集液した膜透過
液を放流領域5に導く導出管15からなり、導出管15
の先端側が放流領域5の水面下に開口するサイフォン管
路をなしており、導出管15の先端開口は放流領域5に
設けた排水管16の開口より深い水深下に位置してい
る。また、反応領域4には、散気装置11へ曝気空気を
供給する手段として水中ブロワ17を浸漬している。
Each of the membrane cartridges 9 of the membrane separation device 7 is a flat membrane type having an organic filtration membrane disposed on the surface of a rigid filter plate, and the membrane permeate flow path of the filter plate communicates with the permeate discharge system 12. doing. The permeated liquid outlet system 12 is a flexible tube 13 that communicates with the membrane permeate flow path of the filter plate, a liquid collection header 14 that collects and connects the tubes 13, and guides the collected liquid permeated liquid to the discharge area 5. The outlet pipe 15
Of the outlet pipe 5 is located below the water surface of the discharge area 5, and the opening of the outlet pipe 15 is located below the water depth of the drain pipe 16 provided in the discharge area 5. In the reaction area 4, an underwater blower 17 is immersed as a means for supplying aerated air to the air diffuser 11.

【0013】上記した構成において、槽体2の反応領域
4に流入した被処理水6は、水中ブロア17から散気装
置11を通して曝気する空気のエアリフト作用を受けて
槽内を循環し、槽内の活性汚泥が空気の酸素を受けて被
処理水6に含まれる有機物を生物学的処理する。また、
エアリフト作用による生起する上昇流が膜分離装置7に
おける膜カートリッジ9の有機濾過膜の膜面に掃流とし
て作用し、膜面に対するケーキ層の付着を抑制する。
In the above-described configuration, the water 6 to be treated flowing into the reaction region 4 of the tank body 2 is circulated in the tank by the air lift effect of the air aerated from the underwater blower 17 through the air diffuser 11, Activated sludge receives oxygen from the air and biologically treats organic substances contained in the water 6 to be treated. Also,
The upward flow generated by the air lift function acts as a scavenging flow on the membrane surface of the organic filtration membrane of the membrane cartridge 9 in the membrane separation device 7 to suppress the adhesion of the cake layer to the membrane surface.

【0014】膜分離装置7は、透過液導出系12がサイ
フォン管路をなすことから、反応領域4における液面と
放流領域5における液面との間における自然水頭ΔH1
を駆動圧力として作動し、膜カートリッジ9の有機濾過
膜を透過した透過液がチューブ13、集液ヘッダー1
4、導出管15を通って放流領域5に流れ出る一方で、
活性汚泥が槽内に残留する。
Since the permeated liquid outlet system 12 forms a siphon pipe, the natural water head ΔH 1 between the liquid surface in the reaction region 4 and the liquid surface in the discharge region 5
Is operated as a driving pressure, and the permeated liquid that has passed through the organic filtration membrane of the membrane cartridge 9 flows through the tube 13 and the collection header 1.
4. While flowing out into the discharge area 5 through the outlet pipe 15,
Activated sludge remains in the tank.

【0015】したがって、槽内の活性汚泥が系外へ流出
しないので、反応領域4における汚泥濃度を高濃度に維
持することができ、被処理液6の槽内滞留時間が短くな
るので、槽体2を搬送可能な小容量の形態に構成するこ
とができる。
Since the activated sludge in the tank does not flow out of the system, the sludge concentration in the reaction zone 4 can be maintained at a high level, and the residence time of the liquid 6 to be treated in the tank is shortened. 2 can be configured in a small capacity form that can be transported.

【0016】図1において二点鎖線18で示すように、
透過液導出系12は、サイフォン管路でなく、大気中に
開放する形態とすることも可能である。しかし、透過液
導出系12を流れる流量は、常時に管路を満たすほどに
流れないので、開口端から大気が管路に流入し、大気圧
が透過液導出系12の最頂部aおいて作用することにな
り、膜分離装置7に駆動圧力として作用する自然水頭Δ
2は、反応領域4における液面と二点鎖線18で示す
透過液導出系12の最頂部aとの間における水頭とな
る。
As shown by a two-dot chain line 18 in FIG.
The permeate outlet system 12 may be open to the atmosphere instead of the siphon line. However, since the flow rate flowing through the permeated liquid outlet system 12 does not always flow so as to fill the conduit, the air flows into the conduit from the open end, and the atmospheric pressure acts on the top a of the permeated liquid outlet system 12. And the natural head Δ acting as a driving pressure on the membrane separation device 7
H 2 becomes a water head between the liquid level in the reaction region 4 and the top a of the permeated liquid outlet system 12 indicated by the two-dot chain line 18.

【0017】したがって、透過液導出系12がサイフォ
ン管路をなすことにより、反応領域4における液面から
膜分離装置7の頂部までの距離に拘わりなく、浅い水深
下にに膜分離装置7を浸漬する場合にあっても、膜分離
装置7の駆動圧力として大きな自然水頭を利用すること
ができる。
Accordingly, since the permeated liquid discharge system 12 forms a siphon pipe, the membrane separation device 7 is immersed under a shallow water depth regardless of the distance from the liquid surface in the reaction region 4 to the top of the membrane separation device 7. Even in this case, a large natural head can be used as the driving pressure of the membrane separation device 7.

【0018】また、散気装置11に空気を供給する手段
として水中ブロア17を槽内に浸漬することにより、ポ
ンプやブロワなどの付帯設備を配置する機械室等の上屋
を設けずとも、ブロワから発生する騒音を抑制すること
ができる。
The submersible blower 17 is immersed in the tank as a means for supplying air to the air diffuser 11, so that a blower can be provided without providing a machine room for installing auxiliary equipment such as a pump and a blower. Noise generated from the vehicle can be suppressed.

【0019】また、ケーシング8が槽体2と一体をなす
ことにより、ケーシング8の下部域をガイドにして曝気
空気を有効に膜カートリッジ9に作用させることができ
るとともに、槽体2の搬送移動に際しても別途固定手段
を設けることなくケーシング3を安定維持できる。
Further, since the casing 8 is formed integrally with the tank 2, the aerated air can be effectively applied to the membrane cartridge 9 by using the lower region of the casing 8 as a guide, and when the tank 2 is transported. Also, the casing 3 can be stably maintained without separately providing fixing means.

【0020】図5は本発明の他の実施の形態を示すもの
であり、先の実施の形態と同様の作用を行なう部材は同
一番号を付して説明を省略する。図5において、槽体2
の内部には、仕切壁3、3を隔てて第1反応領域4aと
第2反応領域4bと放流領域5を区画形成しており、第
1反応領域4aは嫌気性をなし、第2反応領域4bは好
気性をなす。被処理水6が流入する第1反応領域4aと
第2反応領域4bとの間には連通路として越流堰31を
設けており、第2反応領域4bには第1反応領域4aへ
槽内液を供給する水中ポンプ32を浸漬している。尚、
他の構成として、越流堰31を第2反応領域4bから第
1反応領域4aに越流する構成とし、水中ポンプを32
を第1反応領域4aに設けることも可能である。また、
越流堰31に代えて潜流堰を設けることも可能である。
FIG. 5 shows another embodiment of the present invention, in which members having the same functions as those in the previous embodiment are given the same reference numerals and description thereof is omitted. In FIG. 5, the tank 2
Inside, a first reaction region 4a, a second reaction region 4b, and a discharge region 5 are formed with partition walls 3, 3 therebetween, and the first reaction region 4a is anaerobic, and the second reaction region is formed. 4b is aerobic. An overflow weir 31 is provided as a communication passage between the first reaction zone 4a into which the water 6 to be treated flows and the second reaction zone 4b, and the second reaction zone 4b is connected to the first reaction zone 4a. The submersible pump 32 for supplying the liquid is immersed. still,
As another configuration, the overflow weir 31 is configured to overflow from the second reaction region 4b to the first reaction region 4a, and
May be provided in the first reaction region 4a. Also,
It is also possible to provide a submerged weir instead of the overflow weir 31.

【0021】上記した構成においては、第2反応領域4
bの槽内液が硝化液として第1反応領域4aに水中ポン
プ32を通して循環し、第1反応領域4aにおいて脱窒
処理した槽内液が越流堰31を通して第2反応領域4b
に流入する。一方、第2反応領域4bから流出する槽内
液は膜分離装置7を透過して放流領域5へ流れ出るの
で、槽内の活性汚泥が系外へ流出せず、汚泥濃度を高濃
度に維持できるので、搬送可能な小容量の槽体2におい
て脱窒処理を行なうことができる。
In the above configuration, the second reaction region 4
The liquid in the tank b is circulated as a nitrification liquid to the first reaction area 4a through the submersible pump 32, and the liquid in the tank denitrified in the first reaction area 4a is passed through the overflow weir 31 to the second reaction area 4b.
Flows into. On the other hand, the liquid in the tank flowing out of the second reaction area 4b passes through the membrane separation device 7 and flows out to the discharge area 5, so that the activated sludge in the tank does not flow out of the system and the sludge concentration can be maintained at a high concentration. Therefore, the denitrification treatment can be performed in the small-capacity tank body 2 that can be transported.

【0022】また、水中ポンプ32および水中ブロア1
7を槽内に浸漬することにより、ポンプやブロワなどの
付帯設備を配置する機械室等の上屋を設けずとも、ポン
プやブロワから発生する騒音を抑制することができる。
The submersible pump 32 and the submersible blower 1
By immersing 7 in the tank, the noise generated from the pump and the blower can be suppressed without providing a shed such as a machine room in which auxiliary equipment such as a pump and a blower is disposed.

【0023】[0023]

【発明の効果】以上述べたように、本発明によれば、槽
体の内部に反応領域と放流領域を区画形成し、反応領域
に浸漬した膜分離装置で活性汚泥を分離するので、槽内
の活性汚泥濃度を高く維持することができ、槽体を搬送
可能な小容量とすることができる。透過液導出系がサイ
フォン管路をなすことから、浅い水深下に膜分離装置を
浸漬する状態においても、反応領域における液面と放流
領域における液面との間における大きな自然水頭を駆動
圧力とすることができる。水中ブロアおよび水中ポンプ
を槽内に浸漬することにより、ポンプやブロワなどの付
帯設備を配置する機械室等の上屋を設けずとも、ブロワ
やポンプから発生する騒音を抑制することができる。
As described above, according to the present invention, a reaction zone and a discharge zone are defined inside a tank body, and activated sludge is separated by a membrane separation device immersed in the reaction zone. The activated sludge concentration can be kept high, and the tank can be made to have a small capacity that can be transported. Since the permeated liquid discharge system forms a siphon conduit, the driving pressure is the large natural head between the liquid level in the reaction area and the liquid level in the discharge area even when the membrane separation device is immersed under shallow water depth. be able to. By immersing the submersible blower and submersible pump in the tank, the noise generated from the blower and the pump can be suppressed without providing a shed such as a machine room in which ancillary equipment such as the pump and the blower is disposed.

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

【図1】本発明の実施形態における移動式浸漬型膜分離
汚水処理装置の全体構成を示す摸式図である。
FIG. 1 is a schematic diagram showing an overall configuration of a mobile immersion type membrane separation sewage treatment apparatus according to an embodiment of the present invention.

【図2】同膜分離装置の断面図である。FIG. 2 is a sectional view of the membrane separation device.

【図3】図2のA−A矢視断面図である。FIG. 3 is a sectional view taken on line AA of FIG. 2;

【図4】同膜分離装置の斜視図である。FIG. 4 is a perspective view of the membrane separation device.

【図5】本発明の他の実施形態における移動式浸漬型膜
分離汚水処理装置の全体構成を示す摸式図である。
FIG. 5 is a schematic diagram showing an overall configuration of a mobile immersion type membrane separation sewage treatment apparatus according to another embodiment of the present invention.

【図6】従来の汚水処理装置の全体構成を示す摸式図で
ある。
FIG. 6 is a schematic diagram showing the entire configuration of a conventional sewage treatment apparatus.

【符号の説明】[Explanation of symbols]

1 移動式浸漬型膜分離汚水処理装置 2 槽体 3 仕切壁 4 反応領域 5 放流領域 6 被処理水 7 膜分離装置 8 ケーシング 9 膜カートリッジ 10 案内溝 11 散気装置 12 透過液導出系 13 チューブ 14 集液ヘッダー 15 導出管 16 排水管 17 水中ブロワ Reference Signs List 1 mobile immersion type membrane separation sewage treatment apparatus 2 tank body 3 partition wall 4 reaction area 5 discharge area 6 water to be treated 7 membrane separation apparatus 8 casing 9 membrane cartridge 10 guide groove 11 air diffuser 12 permeate extraction system 13 tube 14 Liquid collection header 15 Outlet pipe 16 Drain pipe 17 Submersible blower

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山田 豊 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 (72)発明者 刈谷 一彦 大阪府大阪市中央区南船場4丁目11−20 クボタ環境サービス株式会社内 (72)発明者 川上 進 大阪府大阪市中央区南船場4丁目11−20 クボタ環境サービス株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yutaka Yamada 2-47, Shizitsuhigashi 1-chome, Naniwa-ku, Osaka-shi, Osaka (72) Inventor Kazuhiko Kariya 4--11 Minamisenba, Chuo-ku, Osaka-shi, Osaka −20 Inside Kubota Environmental Service Co., Ltd. (72) Inventor Susumu Kawakami 4-11-20 Minamisenba, Chuo-ku, Osaka City, Osaka Inside Kubota Environmental Service Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 搬送可能なユニット形式をなす槽体の内
部に、仕切壁を隔てて反応領域と放流領域を区画形成
し、被処理水が流入する反応領域にケーシングが槽体と
一体をなす膜分離装置を浸漬し、ケーシング内に複数の
平膜型の膜カートリッジを鉛直方向に平行に配置し、基
端側が膜カートリッジに連通するとともに、先端側が放
流領域に連通する透過液導出系を設け、膜分離装置にお
ける膜カートリッジの下方に散気装置を配置するととも
に、散気装置へ曝気空気を供給する水中ブロワを槽内に
浸漬したことを特徴とする移動式浸漬型膜分離汚水処理
装置。
1. A reaction area and a discharge area are defined inside a tank body having a unit type capable of being conveyed with a partition wall therebetween, and a casing is integrated with the tank body in a reaction area into which water to be treated flows. A membrane separation device is immersed, a plurality of flat membrane type membrane cartridges are arranged in the casing in parallel in the vertical direction, and a permeated liquid discharge system is provided in which the proximal end communicates with the membrane cartridge and the distal end communicates with the discharge area. A mobile immersion type membrane separation sewage treatment apparatus, wherein an air diffuser is disposed below a membrane cartridge in the membrane separator, and an underwater blower for supplying aeration air to the air diffuser is immersed in a tank.
【請求項2】 搬送可能なユニット形式をなす槽体の内
部に、仕切壁を隔てて第1反応領域と第2反応領域と放
流領域を区画形成し、被処理水が流入する第1反応領域
と第2反応領域との間に連通路を設け、第1反応領域と
第2反応領域の何れか一方の反応領域に、他方の反応領
域へ槽内液を供給する水中ポンプを浸漬し、第2反応領
域にケーシングが槽体と一体をなす膜分離装置を浸漬
し、ケーシング内に複数の平膜型の膜カートリッジを鉛
直方向に平行に配置し、基端側が膜カートリッジに連通
するとともに、先端側が放流領域に連通する透過液導出
系を設け、膜分離装置における膜カートリッジの下方に
散気装置を配置するとともに、散気装置へ曝気空気を供
給する水中ブロワを槽内に浸漬したことを特徴とする移
動式浸漬型膜分離汚水処理装置。
2. A first reaction area into which water to be treated flows is formed by partitioning a first reaction area, a second reaction area, and a discharge area with a partition wall therebetween in a tank having a unit type capable of being transported. A communication path is provided between the first reaction region and the second reaction region, and a submersible pump that supplies the tank solution to the other reaction region is immersed in one of the first reaction region and the second reaction region. (2) A membrane separation device in which a casing is integrated with a tank body is immersed in the reaction area, and a plurality of flat membrane type membrane cartridges are arranged in the casing in parallel in the vertical direction. A permeated liquid outlet system that communicates with the discharge area on the side is provided.A diffuser is arranged below the membrane cartridge in the membrane separator, and an underwater blower that supplies aerated air to the diffuser is immersed in the tank. Mobile immersion type membrane separation sewage Processing equipment.
【請求項3】 膜透過液流路が先端側において放流領域
の水面下に開口するサイフォン管路をなすことを特徴と
する請求項1または2記載の移動式浸漬型膜分離汚水処
理装置。
3. The mobile immersion type membrane separation sewage treatment apparatus according to claim 1, wherein the membrane permeated liquid flow path forms a siphon pipe which is opened below the water surface in the discharge area on the distal end side.
JP06023298A 1998-03-12 1998-03-12 Mobile immersion type membrane separation sewage treatment equipment Expired - Lifetime JP3506603B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06023298A JP3506603B2 (en) 1998-03-12 1998-03-12 Mobile immersion type membrane separation sewage treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06023298A JP3506603B2 (en) 1998-03-12 1998-03-12 Mobile immersion type membrane separation sewage treatment equipment

Publications (2)

Publication Number Publication Date
JPH11253942A true JPH11253942A (en) 1999-09-21
JP3506603B2 JP3506603B2 (en) 2004-03-15

Family

ID=13136235

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06023298A Expired - Lifetime JP3506603B2 (en) 1998-03-12 1998-03-12 Mobile immersion type membrane separation sewage treatment equipment

Country Status (1)

Country Link
JP (1) JP3506603B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010081291A (en) * 2000-02-11 2001-08-29 조덕희 a wastewater treatment equipment
JP2004351247A (en) * 2003-05-27 2004-12-16 Yanmar Co Ltd Portable type sewage treatment unit and construction method of this portable type sewage treatment unit
US7264727B2 (en) * 2003-01-25 2007-09-04 Holt Karl K Septic system remediation method and apparatus
US7468135B2 (en) 2003-01-25 2008-12-23 Engineered Solutions, Inc. Portable tank wastewater treatment system and method
US7718067B2 (en) 2005-05-19 2010-05-18 Aero-Stream, Llc Septic system remediation method and apparatus
EP2298703A1 (en) 2004-04-07 2011-03-23 University College Cardiff Consultants LTD. Treatment of saltwater-based domestic wastewater

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58146600U (en) * 1982-03-23 1983-10-01 大金興業株式会社 Mobile sewage treatment equipment
JPH04131182A (en) * 1990-09-20 1992-05-01 Ebara Infilco Co Ltd Biological treating device for organic polluted water
JPH05168864A (en) * 1991-12-19 1993-07-02 Ebara Infilco Co Ltd Membrane filter
JPH08196874A (en) * 1995-01-30 1996-08-06 Mitsubishi Rayon Co Ltd Moving type pool water purifying device
JPH091173A (en) * 1995-06-26 1997-01-07 Matsushita Electric Works Ltd Waste water treatment equipment

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58146600U (en) * 1982-03-23 1983-10-01 大金興業株式会社 Mobile sewage treatment equipment
JPH04131182A (en) * 1990-09-20 1992-05-01 Ebara Infilco Co Ltd Biological treating device for organic polluted water
JPH05168864A (en) * 1991-12-19 1993-07-02 Ebara Infilco Co Ltd Membrane filter
JPH08196874A (en) * 1995-01-30 1996-08-06 Mitsubishi Rayon Co Ltd Moving type pool water purifying device
JPH091173A (en) * 1995-06-26 1997-01-07 Matsushita Electric Works Ltd Waste water treatment equipment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010081291A (en) * 2000-02-11 2001-08-29 조덕희 a wastewater treatment equipment
US7264727B2 (en) * 2003-01-25 2007-09-04 Holt Karl K Septic system remediation method and apparatus
US7468135B2 (en) 2003-01-25 2008-12-23 Engineered Solutions, Inc. Portable tank wastewater treatment system and method
JP2004351247A (en) * 2003-05-27 2004-12-16 Yanmar Co Ltd Portable type sewage treatment unit and construction method of this portable type sewage treatment unit
EP2298703A1 (en) 2004-04-07 2011-03-23 University College Cardiff Consultants LTD. Treatment of saltwater-based domestic wastewater
US7718067B2 (en) 2005-05-19 2010-05-18 Aero-Stream, Llc Septic system remediation method and apparatus

Also Published As

Publication number Publication date
JP3506603B2 (en) 2004-03-15

Similar Documents

Publication Publication Date Title
JPH11165200A (en) Method for treating sludge
JP2011110520A (en) Apparatus for treating organic waste water and method of treating organic waste water
JPH11300177A (en) Membrane separator
US11643345B2 (en) Method for treating organic wastewater, and device for treating organic wastewater
JP3963497B2 (en) Organic wastewater treatment method and apparatus
JP4702749B2 (en) Water treatment equipment
JPH11253942A (en) Immersion type mobile membrane separation wastewater treatment apparatus
JP2007098368A (en) Immersed-membrane separation apparatus and method therefor
JP2006205155A (en) Anaerobic tank and waste water treatment system including the same
JP2003117578A (en) Repairing method for bioreaction region in biotreatment equipment for sewage
JP2006007033A (en) Biological treatment tank for waste water and biologically treating method
JPH1085788A (en) Nitrification and denitrification method
JPH10296252A (en) Aeration tank immersed membrane separation activated sludge apparatus
JPH09117794A (en) Biological denitrification device
JP3083991B2 (en) Merger treatment purification equipment
JP2017104780A (en) Conversion method and renewal method of biological treatment apparatus
KR20040020325A (en) A method for treating the graywater by membrane
KR102614473B1 (en) Sewage Treatment System equipped with MBR
US20180251389A1 (en) Home sewage treatment system
JP2001170674A (en) Treating device for high-concentration sewage
KR20010074162A (en) Foul drain processing unit and method using settling chamber and biofilm filteration aquarium
JP2000051889A (en) Sewage treatment equipment
JP3652051B2 (en) Wastewater treatment equipment
JPH10296251A (en) Method for regulating sludge in sewage treatment tank
KR101044350B1 (en) Water treatment apparatus

Legal Events

Date Code Title Description
A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20031216

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

Free format text: PAYMENT UNTIL: 20081226

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20081226

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20091226

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20091226

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20101226

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20101226

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20111226

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20111226

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20121226

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20121226

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20131226

Year of fee payment: 10

EXPY Cancellation because of completion of term