JP2003313917A - Circulatory purifier - Google Patents

Circulatory purifier

Info

Publication number
JP2003313917A
JP2003313917A JP2003060724A JP2003060724A JP2003313917A JP 2003313917 A JP2003313917 A JP 2003313917A JP 2003060724 A JP2003060724 A JP 2003060724A JP 2003060724 A JP2003060724 A JP 2003060724A JP 2003313917 A JP2003313917 A JP 2003313917A
Authority
JP
Japan
Prior art keywords
water
tank
membrane
flush
toilet
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
JP2003060724A
Other languages
Japanese (ja)
Other versions
JP3734478B2 (en
Inventor
Yutaka Kojima
豊 小島
Hisaya Suzuki
久也 鈴木
Masahiro Tanida
昌大 谷田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
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 JP2003060724A priority Critical patent/JP3734478B2/en
Publication of JP2003313917A publication Critical patent/JP2003313917A/en
Application granted granted Critical
Publication of JP3734478B2 publication Critical patent/JP3734478B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

  • Sanitary Device For Flush Toilet (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a circulatory purifier capable of completely making solid- liquid separation of sanitary wastewater decomposed with the bacteria to purify into clean water without containing any impurity, circulating the water to reuse it as flush water and using it as washing water for cleaning a toilet room or washing a circulatory septic tank. <P>SOLUTION: The circulatory purifier 1 installed in a flush toilet or a small flush toilet temporary room or the existing toilet room includes a decomposed settling tank 2 for decomposing the sanitary wastewater with the bacteria and making settling separation of decomposed sludge and water, a membrane separating tank 4 filtering top supplied from the decomposed settling tank 2 by means of a first pumping device 11 by a membrane separator 14 placed inside of the tank, a circulation system is formed of a water storage tank 3 for storing treated water by the membrane separating tank 4 and a second pumping device 23 for supplying the water in the water storage tank 3 as flush water and a water sharing means 26 for taking out the water in the water storage tank 3 as washing water to the second pumping device 23. <P>COPYRIGHT: (C)2004,JPO

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】この発明は、水洗式又は簡易
水洗式の仮設便所や既設の便所に設置されて、生物処理
と膜分離とを使用して汚水を浄化し、浄化された水を再
び水洗に使用されるように循環させる循環式浄化装置に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is installed in a flush toilet or a simple flush toilet or an existing toilet to purify sewage using biological treatment and membrane separation, and to purify the purified water again. The present invention relates to a circulation type purification device which circulates so as to be used for washing.

【0002】[0002]

【従来の技術】工事現場や各種イベント会場、或いは、
海水浴場等に設置されている仮設便所は、最近は環境衛
生の問題から便尿貯槽式に替わって水洗式又は簡易水洗
式のものが主流になっている。こうした水洗式の仮設便
所には、その下部に汚水を貯留しておく便槽が設置され
ており、ある程度汚水が留ると汲取ってし尿処理場に運
んだり、又、浄化槽等を設置してあるものは水処理後放
水していた。
2. Description of the Related Art Construction sites, various event venues, or
Temporary toilets installed at beaches and the like have recently become flush-type or simple flush-type instead of the fecal urine storage type because of environmental hygiene issues. These flush-type temporary toilets are equipped with a toilet tank for storing dirty water at the bottom of the toilet, and when dirty water is retained to some extent, they are taken to a urine treatment plant or a septic tank is installed. Some had been discharged after water treatment.

【0003】ところが、このような水洗式や簡易水洗式
の仮設便所の場合も旧来の貯槽式便所と同様に留まった
汚水から悪臭が発生するため、脱臭装置等の付属設備を
設けなければならず、又、水で流すものであるため、便
槽は相当に大きなものを設置しなければならなかった。
However, even in the case of such a flush toilet or a simple flush toilet, an odor is generated from the accumulated sewage as in the case of the conventional storage-type toilet, so an auxiliary equipment such as a deodorizing device must be provided. Also, because it is flushed with water, a large toilet bowl had to be installed.

【0004】また、浄化槽を設置するものにあっては、
型式認定品を使用しなければ放流することはできなかっ
た。そのため、設置スペースの問題や設置コストの問題
が多く、水洗化の普及は難しいのが現状である。
Also, in the case of installing a septic tank,
It could not be discharged without using a type-approved product. Therefore, there are many problems of installation space and installation cost, and it is currently difficult to popularize washing with water.

【0005】その後、こうした欠点を解消すべく、実開
平7−9494号に開示されているもののごとく、バク
テリアを使用して汚物を分解することで汚水を浄化しな
がら、垂下壁と立設壁とからなる区画壁の間を複数回通
水させる間に分解された汚泥と上澄み水とに沈降させて
分離し、その上澄み水を再び水洗に使用されるように循
環させることで、水洗の水を再利用できるようにし、使
用する水を節減し、悪臭の発生をなくした循環式浄化槽
が提供されるようになった。
After that, in order to eliminate these drawbacks, as disclosed in Japanese Utility Model Laid-Open No. 7-9494, bacteria are used to decompose filth to purify sewage, while the drooping wall and the standing wall are separated. The sludge and the supernatant water that have been decomposed while passing water between the partition walls consisting of 2) are separated and separated, and the supernatant water is circulated so that it can be reused for washing, Circulating septic tanks have been provided that are reusable, use less water, and eliminate foul odors.

【0006】[0006]

【発明が解決しようとする課題】しかし、このような循
環式浄化槽では、汚泥と上澄み水との沈降による分離に
よってのみ固液分離を行っているため、十分に分離がな
されず、未だ不純物が混入した状態の水が水洗タンクに
流入してしまうという欠点があった。また、工事現場や
各種イベント会場、或いは、海水浴場等においては水源
が確保できないので、仮設便所の清掃時や仮設便所の撤
去時に必要な洗浄水を十分に確保することが困難であっ
た。
However, in such a circulation type septic tank, solid-liquid separation is performed only by separation of sludge and supernatant water by sedimentation, so that sufficient separation is not made and impurities are still mixed. There was a drawback that the water in the filled state would flow into the flush tank. Further, since it is not possible to secure a water source at the construction site, various event venues, beaches, etc., it was difficult to secure sufficient washing water when cleaning the temporary toilet or removing the temporary toilet.

【0007】本発明は、上述した問題点等に鑑み、バク
テリアによって分解された汚水を完全に固液分離して、
不純物を含まない澄んだ水に浄化し、その水を循環させ
て水洗の水として再利用できるようにし、かつ便所の清
掃や循環式浄化槽の洗浄時の洗浄水として利用できるよ
うにした循環式浄化装置を提供することを目的とする。
In view of the above-mentioned problems and the like, the present invention completely solid-liquid separates wastewater decomposed by bacteria,
Recycling purification that purifies the water without impurities and circulates it so that it can be reused as water for rinsing, and can also be used as cleaning water when cleaning toilets or cleaning recirculating septic tanks. The purpose is to provide a device.

【0008】[0008]

【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に係る本発明の循環式浄化装置は、水
洗式或いは簡易水洗式の仮設便所や既設の便所に設置さ
れる循環式浄化装置であって、バクテリアによる汚物の
分解と分解された汚泥と水との沈降分離とを行う分解沈
降槽と、第1の汲上げ装置により分解沈降槽から供給す
る上澄み水を槽内に配置した膜分離装置で濾過する膜分
離槽と、膜分離槽で処理した水を貯水する貯留槽と、貯
留槽の水を水洗水として供給する第2の汲上げ装置とで
循環系を形成し、第2の汲上げ装置に貯留槽の水を洗浄
水として取り出す分水手段を設けたものである。
In order to solve the above-mentioned problems, the circulation type purifying apparatus of the present invention according to claim 1 is a circulation type installed in a flush or simple flush type temporary toilet or an existing toilet. A decontamination tank for decomposing filth caused by bacteria and sedimentation and separation of decomposed sludge and water, and a supernatant water supplied from the decomposition and sedimentation tank by the first pumping device into the tank. A circulation system is formed by a membrane separation tank for filtering with the membrane separation device arranged, a storage tank for storing water treated in the membrane separation tank, and a second pumping device for supplying water from the storage tank as washing water. The second pumping device is provided with water diversion means for taking out water in the storage tank as washing water.

【0009】また、請求項2に係る本発明の循環式浄化
装置は、膜分離装置が分解沈降槽から供給する上澄み水
を膜分離槽内の水頭を駆動力として濾過する膜浸漬体
と、膜浸漬体の下方に設置する曝気装置とを有するもの
である。
Further, in the circulation type purification apparatus of the present invention according to claim 2, a membrane dipping body for filtering the supernatant water supplied from the decomposition and settling tank by the membrane separation apparatus by using the head of the membrane separation tank as a driving force, and the membrane. And an aeration device installed below the immersion body.

【0010】[0010]

【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、循環式浄化
装置1は仮設便所Aの下部及び背面部に取付けたり、又
は分離して設置している。循環式浄化装置1は主に分解
沈降槽2と貯留槽3、膜分離槽4により構成している。
分解沈降槽2と貯留槽3とは、合成樹脂等からなる一体
の槽に組み込むと共に、夫々密閉された槽として区画壁
29により隔絶した状態に形成している。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. 1 to 4, the circulation type purifying apparatus 1 is attached to the lower portion and the back portion of the temporary toilet A, or is installed separately. The circulation type purification device 1 mainly comprises a decomposition settling tank 2, a storage tank 3, and a membrane separation tank 4.
The decomposition / sedimentation tank 2 and the storage tank 3 are incorporated into an integrated tank made of synthetic resin or the like, and are formed in a separated state by partition walls 29 as sealed tanks.

【0011】分解沈降槽2の槽内は、区画壁によって複
数の区画室5に区画しており、区画室5は、便所からの
汚水が最初に流入する第1の区画室5a、これに隣接し
て次に水が流入する第2の区画室5b、これに隣接して
最後に水が流入する第3の区画室5cの3つに構成して
いる。第1、第2の区画室5a、5bにはバクテリアを
付着させた菌付着床材6を充填している。尚、区画室5
a、5bを省略し、区画室5cに直接汚水を流入させる
ことも可能である。
The inside of the decomposition settling tank 2 is divided into a plurality of compartments 5 by compartment walls, and the compartment 5 is adjacent to the first compartment 5a into which the dirty water from the toilet first flows. Then, there are three second compartments 5b into which water flows in next, and a third compartment 5c adjacent to which the water finally flows in. The first and second compartments 5a and 5b are filled with a bacterium-adhered bed material 6 to which bacteria are attached. In addition, compartment 5
It is also possible to omit a and 5b and to directly flow the sewage into the compartment 5c.

【0012】前記区画壁は、分解沈降槽2の天板7から
垂下した垂下壁8と分解沈降槽2の底板9に立設した立
設壁10とを適宜間隔をあけて並設すると共に、垂下壁
8と底板9との間、及び立設壁10と天板7との間に適
宜隙間を持たせている。
The partition wall includes a hanging wall 8 hanging from a top plate 7 of the decomposition settling tank 2 and a standing wall 10 standing on a bottom plate 9 of the decomposition settling tank 2 and arranged in parallel with each other at appropriate intervals. Appropriate gaps are provided between the hanging wall 8 and the bottom plate 9 and between the standing wall 10 and the top plate 7.

【0013】この分解沈降槽2では第1の区画室5aに
流入した汚水を菌付着床材6のバクテリアによって分解
し、分解した汚泥が第1の区画室5aの底に沈降し、区
画室5aの水位が増加して立設壁10を越えると隣接す
る第2の区画室5bに上澄み水が流れ込む。第2の区画
室5bにおいてもこれと同じく分解と沈降が生じて第3
の区画室5cに上澄み水が至る。
In the decomposition / sedimentation tank 2, the wastewater that has flowed into the first compartment 5a is decomposed by the bacteria of the bed material 6 to which the bacteria have adhered, and the decomposed sludge settles on the bottom of the first compartment 5a, and the compartment 5a. When the water level increases, and the water exceeds the standing wall 10, the clear water flows into the adjacent second compartment 5b. Similarly, in the second compartment 5b, decomposition and sedimentation occur and the third compartment
The clear water reaches the compartment 5c.

【0014】ここで、分解沈降槽2の区画の一例を図4
及び図5に示すと、平面形状長方形の分解沈降槽2内の
略中央部に平面形状長方形の第1の区画室5aを配置
し、この第1の区画室5aの図面上の右側面及び下側面
に接してこれを取り囲む部分に平面形状略L字形の第2
の区画室5bを配置し、残る部分に平面形状略L字形の
第3の区画室5cを配置している。前記垂下壁8と立設
壁10とにより第1の区画室5aと第2の区画室5bと
の間及び第2の区画室5bと第3の区画室5cとを区画
し、第1の区画室5aと第3の区画室5cとの間は水が
移動しないように完全に区切っている。
Here, an example of a section of the decomposition settling tank 2 is shown in FIG.
And, as shown in FIG. 5, a first rectangular compartment 5a having a rectangular plan shape is arranged at a substantially central portion in the decomposition and settling tank 2 having a rectangular rectangular shape. The second L-shaped planar shape is provided on the side surface which is in contact with and surrounds the side surface.
The compartment 5b is arranged, and the third compartment 5c having a substantially L-shaped plane is arranged in the remaining portion. The hanging wall 8 and the standing wall 10 partition between the first compartment 5a and the second compartment 5b and between the second compartment 5b and the third compartment 5c, and the first compartment The chamber 5a and the third compartment 5c are completely partitioned so that water does not move.

【0015】したがって、分解沈降槽2内の中央の第1
の区画室5aに流入した水は、図面上右側の第2の区画
室5bに流れ込み、次いで分解沈降槽2の右下角隅部を
曲がって左側の第3の区画室5cに流れ込むことにな
る。尚、上記区画室5の配列、及び水の移動経路は、あ
くまでも一例であるのでそれに限定されることはない。
Therefore, the central first inside the decomposition settling tank 2
The water that has flowed into the compartment 5a flows into the second compartment 5b on the right side in the drawing, then bends through the lower right corner of the decomposition settling tank 2 and flows into the third compartment 5c on the left side. It should be noted that the arrangement of the compartments 5 and the movement path of water are merely examples, and are not limited thereto.

【0016】第3の区画室5cには、第2の区画室5b
との間の立設壁10から最も遠い位置に第1の汲上げ装
置11を設置している。この第1の汲上げ装置11は、
第3の区画室5c内に配置する第1の水中ポンプ12と
この水中ポンプ12によって汲上げる水を膜分離槽4に
送る送水パイプ13とからなる。水中ポンプ12は液面
制御スイッチを有しており、液面制御スイッチは第3の
区画室5c内の水位が第2の区画室5bとの間の立設壁
10を越えないように水中ポンプ12の起動を制御する
のと同時に、水位が所定位置まで下がった際に汲上げを
停止する。
The third compartment 5c has a second compartment 5b.
The 1st pumping apparatus 11 is installed in the position farthest from the standing wall 10 between. This first pumping device 11 is
It is composed of a first submersible pump 12 arranged in the third compartment 5c and a water supply pipe 13 for sending water pumped by the submersible pump 12 to the membrane separation tank 4. The submersible pump 12 has a liquid level control switch. The liquid level control switch prevents the water level in the third compartment 5c from exceeding the standing wall 10 between the third compartment 5c and the second compartment 5b. At the same time as controlling the activation of 12, pumping is stopped when the water level drops to a predetermined position.

【0017】膜分離槽4は送水パイプ13を通って分解
沈降槽2から送られた水が適宜量まで貯留可能な縦長の
密閉された水槽であり、内部に膜分離装置14を設置し
ている。膜分離装置14は、水等の小さな分子のみが透
過できる膜を枠材の両面に張設して形成された複数の膜
浸漬体15を膜分離槽4内の中央に垂直に設置し、膜分
離槽4の水頭を駆動力として膜浸漬体15を透過した水
を集水して貯留槽3に送水する集水装置16を各膜浸漬
体15の上部に取り付ており、各膜浸漬体15から出た
膜透過水は各膜浸漬体上部ノズルからチューブを経て集
水装置16に集まる。膜浸漬体15の下方には曝気装置
17を設置している。本実施の形態では膜濾過の駆動力
は水頭(正圧)濾過で行っているが、ポンプによる吸引
(負圧)濾過でもよい。
The membrane separation tank 4 is a vertically long closed water tank capable of storing an appropriate amount of water sent from the decomposition / sedimentation tank 2 through the water supply pipe 13, and has a membrane separation device 14 installed therein. . The membrane separation device 14 vertically installs a plurality of membrane dipping bodies 15 formed by stretching a membrane permeable to only small molecules such as water on both sides of a frame material in the center of the membrane separation tank 4, A water collecting device 16 that collects the water that has permeated the membrane immersion body 15 by using the water head of the separation tank 4 as a driving force and sends the collected water to the storage tank 3 is attached to the upper portion of each membrane immersion body 15. The permeated water from the membrane 15 is collected from the upper nozzle of each membrane immersion body through the tube to the water collecting device 16. An aeration device 17 is installed below the membrane immersion body 15. In the present embodiment, the driving force for membrane filtration is head (positive pressure) filtration, but suction (negative pressure) filtration by a pump may be used.

【0018】膜分離装置14は、集水装置16によって
膜浸漬体15を透過した水のみを集水し、送水パイプ3
0の途中に設けた滅菌装置31を通過して貯留槽3に送
水することにより、被処理水を完全に生物処理及び固液
分離するものである。曝気装置17、28は振動しなが
ら上昇する散気によって膜浸漬体15を洗浄して膜の目
詰まりを防ぐと共に、生物処理のための酸素を供給す
る。
The membrane separating device 14 collects only the water that has permeated the membrane-immersed body 15 by the water collecting device 16, and the water supply pipe 3
The water to be treated is completely biologically treated and solid-liquid separated by passing the water through the sterilizer 31 provided in the middle of 0 to the storage tank 3. The aeration devices 17 and 28 clean the membrane dip 15 by the air diffused while vibrating to prevent the membrane from being clogged, and supply oxygen for biological treatment.

【0019】本実施の形態の膜分離装置14では、最大
容量370リットルの膜分離槽4に対し有効濾過面積
0.4平方メートル膜浸漬体を5枚設置しており、その
処理能力は1時間当たり42リットル程度である。
In the membrane separation apparatus 14 of this embodiment, five membrane dipping bodies with an effective filtration area of 0.4 square meters are installed in the membrane separation tank 4 having a maximum capacity of 370 liters, and the treatment capacity is 1 hour. It is about 42 liters.

【0020】また、膜分離槽4の上部側壁には水量が適
宜量を越えると越流させて放出する越流パイプ18を設
けており、底部にはコック20によって開閉可能で撤去
時や清掃時に槽内の水を排出する排水パイプ19を設け
ており、これらは一本の放水パイプ21に合流して分解
沈降槽2に至る。
Further, an overflow pipe 18 is provided on the upper side wall of the membrane separation tank 4 for overflowing and discharging when the amount of water exceeds an appropriate amount, and a bottom portion can be opened and closed by a cock 20 at the time of removal or cleaning. A drainage pipe 19 for discharging the water in the tank is provided, and these are joined to one water discharge pipe 21 to reach the decomposition / sedimentation tank 2.

【0021】貯留槽3は膜分離槽4で浄化再生された水
を貯留するものであり、貯留槽3の槽内には内部の水を
仮設便所Aの水洗水に使用すべく水洗タンク22に汲上
げる第2の汲上げ装置23を配置している。第2の汲上
げ装置23は貯留槽3内に配置する第2の水中ポンプ2
4とこの水中ポンプ24によって汲上げる水を水洗タン
ク22に送水する送水パイプ25とからなる。
The storage tank 3 stores the water purified and regenerated in the membrane separation tank 4, and the storage tank 3 is provided with a flush tank 22 in order to use the internal water as flush water for the temporary toilet A. A second pumping device 23 for pumping is arranged. The second pumping device 23 is the second submersible pump 2 arranged in the storage tank 3.
4 and a water supply pipe 25 for sending water to be pumped by the submersible pump 24 to the washing tank 22.

【0022】水洗タンク22にはタンク内の水位を検知
する給水検知機構を設置しており、この給水検知機構と
水中ポンプ24の作動が連動することで、水洗タンク内
22の水がなくなると水中ポンプ24が作動し、自動的
に水洗タンク22に水を汲上げる。
The flush tank 22 is provided with a water supply detection mechanism for detecting the water level in the tank, and the water supply detection mechanism and the operation of the submersible pump 24 are interlocked with each other, so that when the water in the flush tank 22 runs out of water, The pump 24 operates to automatically draw water into the washing tank 22.

【0023】送水パイプ25は途中で分解沈降槽2に至
るリターンパイプ26が分岐し、分岐部に設けた切替コ
ック27とリターンパイプ26とで分水手段を構成して
いる。仮設便所Aの撤去時や清掃時には切替コック27
を操作することで槽内の水を分解沈降槽2に排出し、洗
浄水として利用する。分水手段のリターンパイプ26の
先端を仮設便所Aの付近に設けることで、槽内の水を便
所の清掃時の洗浄水として供給することもできる。
A return pipe 26 reaching the decomposition / sedimentation tank 2 is branched on the way of the water supply pipe 25, and a switching cock 27 and a return pipe 26 provided at the branch portion constitute a water dividing means. Switching cock 27 when removing or cleaning temporary toilet A
Is operated to discharge the water in the tank to the decomposition and settling tank 2 and use it as washing water. By providing the tip of the return pipe 26 of the water diversion means in the vicinity of the temporary toilet A, the water in the tank can be supplied as cleaning water when cleaning the toilet.

【0024】本実施の形態の貯留槽3の容量は膜分離槽
4の処理能力が1時間当たり42リットルであるのに対
し、その約6倍に設定している。一方、水洗タンク22
の容量は約10リットルに設定しているので、貯留槽3
は膜分離装置4の固液処理の処理スピードを補って、水
洗に使用する水が十分に間に合うようにしている。ま
た、簡易水洗式便所にあっては使用水量は更に下がるの
で追従して装置をコンパクトにすることが可能である。
The capacity of the storage tank 3 of this embodiment is set to about 6 times that of the membrane separation tank 4 which has a processing capacity of 42 liters per hour. On the other hand, the washing tank 22
The capacity of the storage tank 3 is set to about 10 liters.
Compensates for the solid-liquid processing speed of the membrane separation device 4 so that the water used for washing is sufficiently in time. Further, in the simple flush toilet, the amount of water used further decreases, so that the device can be made compact by following it.

【0025】[0025]

【発明の効果】上述したように本発明によれば、水洗に
使用された汚物を含む水を生物分解と沈降分離と膜分離
によって処理して不純物を含まない澄んだ水に浄化して
循環させて水洗の水として再利用することで、水源のな
い場所においても水洗式或いは簡易水洗式の仮設便所を
設置でき、あるいは便所の清掃や循環式浄化槽の洗浄時
の洗浄水として利用することで、水源のない場所におい
ても便所の清掃や循環式浄化槽の洗浄を容易に行うこと
ができる。
As described above, according to the present invention, water containing filth used for washing is treated by biodegradation, sedimentation separation and membrane separation to be purified water which is free of impurities and circulated. By reusing as wash water, it is possible to set up a flush toilet or a simple flush toilet even in a place with no water source, or by using it as flush water when cleaning the toilet or cleaning the circulation septic tank, Even in a place where there is no water source, it is possible to easily clean the toilet and the circulating septic tank.

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

【図1】本発明の実施の形態における仮設便所に設置し
た状態の概略図である。
FIG. 1 is a schematic diagram of a state of being installed in a temporary toilet according to an embodiment of the present invention.

【図2】同実施の形態の側面図である。FIG. 2 is a side view of the same embodiment.

【図3】同実施の形態の背面図である。FIG. 3 is a rear view of the same embodiment.

【図4】同実施の形態の分解沈降槽及び貯留槽の横断面
図である。
FIG. 4 is a cross-sectional view of the decomposition settling tank and the storage tank of the same embodiment.

【図5】図4におけるA−A矢視線断面図である。5 is a cross-sectional view taken along the line AA in FIG.

【符号の説明】[Explanation of symbols]

1 循環式浄化装置 2 分解沈降槽 3 貯留槽 4 膜分離槽 5 区画室 5a第1の区画室 5b 第2の区画室 5c 第3の区画室 6 菌付着床材 7 天板 8 垂下壁 9 底板 10 立設壁 11 汲上げ装置 12 水中ポンプ 13 送水パイプ 14 膜分離装置 15 膜浸漬体 16 集水装置 17 曝気装置 18 越流パイプ 19 排水パイプ 20 コック 21 放水パイプ 22 水洗タンク 23 汲上げ装置 24 水中ポンプ 25 送水パイプ 26 リターンパイプ 27 切替コック 28 曝気装置モーター 29 区画壁 30 送水パイプ 31 滅菌装置 32 曝気パイプ A 仮設便所 1 Circulation type purifier 2 Decomposition sedimentation tank 3 storage tanks 4 membrane separation tank 5 compartments 5a first compartment 5b Second compartment 5c Third compartment 6 Bacterial floor material 7 Top plate 8 hanging wall 9 Bottom plate 10 standing wall 11 Pumping device 12 Submersible pump 13 Water supply pipe 14 Membrane separation device 15 Membrane soaker 16 Water collecting device 17 Aerator 18 Overflow pipe 19 drainage pipe 20 cooks 21 Water discharge pipe 22 Washing tank 23 Pumping device 24 Submersible pump 25 water pipe 26 Return pipe 27 Switch cock 28 Aerator motor 29 partition walls 30 water pipe 31 Sterilizer 32 Aeration pipe A temporary toilet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 谷田 昌大 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ水処理技術部内 Fターム(参考) 2D039 AC09 AC11 DA00 4D003 AA01 AB13 BA02 CA03 DA19 FA06 4D006 GA07 HA41 HA93 HA95 JA31Z JA71 KA01 KA43 KB22 KB25 KC14 MA03 PA01 PB08 4D027 AA06    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Masahiro Yata             2-47 Shikitsuhigashi, Naniwa-ku, Osaka-shi, Osaka             Kubota Water Treatment Engineering Department F-term (reference) 2D039 AC09 AC11 DA00                 4D003 AA01 AB13 BA02 CA03 DA19                       FA06                 4D006 GA07 HA41 HA93 HA95 JA31Z                       JA71 KA01 KA43 KB22 KB25                       KC14 MA03 PA01 PB08                 4D027 AA06

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水洗式或いは簡易水洗式の仮設便所や既
設の便所に設置される循環式浄化装置であって、バクテ
リアによる汚物の分解と分解された汚泥と水との沈降分
離とを行う分解沈降槽と、第1の汲上げ装置により分解
沈降槽から供給する上澄み水を槽内に配置した膜分離装
置で濾過する膜分離槽と、膜分離槽で処理した水を貯水
する貯留槽と、貯留槽の水を水洗水として供給する第2
の汲上げ装置とで循環系を形成し、第2の汲上げ装置に
貯留槽の水を洗浄水として取り出す分水手段を設けたこ
とを特徴とする循環式浄化装置。
1. A circulating type purification device installed in a flush or simple flush type temporary toilet or an existing toilet, which decomposes sewage by bacteria and sedimentation and separation of decomposed sludge and water. A settling tank, a membrane separation tank for filtering the supernatant water supplied from the decomposition settling tank by the first pumping device by a membrane separation device arranged in the tank, and a storage tank for storing the water treated in the membrane separation tank, Second supply of water from storage tank as flush water
And a pumping device for forming a circulation system, and the second pumping device is provided with water diversion means for taking out water in the storage tank as washing water.
【請求項2】 膜分離装置が分解沈降槽から供給する上
澄み水を膜分離槽内の水頭を駆動力として濾過する膜浸
漬体と、膜浸漬体の下方に設置する曝気装置とを有する
ことを特徴とする請求項1に記載の循環式浄化装置。
2. The membrane separator has a membrane dip that filters the supernatant water supplied from the decomposition and settling tank using the water head in the membrane separation tank as a driving force, and an aerator installed below the membrane dip. The circulating purification apparatus according to claim 1, which is characterized in that.
JP2003060724A 2003-03-07 2003-03-07 Circulating purification device Expired - Fee Related JP3734478B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003060724A JP3734478B2 (en) 2003-03-07 2003-03-07 Circulating purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003060724A JP3734478B2 (en) 2003-03-07 2003-03-07 Circulating purification device

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP34805895A Division JP3449849B2 (en) 1995-12-15 1995-12-15 Circulating purification system

Publications (2)

Publication Number Publication Date
JP2003313917A true JP2003313917A (en) 2003-11-06
JP3734478B2 JP3734478B2 (en) 2006-01-11

Family

ID=29546050

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3734478B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102351373A (en) * 2011-07-06 2012-02-15 北京市环境保护科学研究院 Environmental protection toilet flushed by circulating water and toilet sewage processing method
JP2021030152A (en) * 2019-08-23 2021-03-01 オシュン株式会社 Water treatment system and water treatment method
CN113864888A (en) * 2020-06-30 2021-12-31 青岛海尔空调器有限总公司 Water tank structure for water washing module, water washing module and air conditioner

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102351373A (en) * 2011-07-06 2012-02-15 北京市环境保护科学研究院 Environmental protection toilet flushed by circulating water and toilet sewage processing method
JP2021030152A (en) * 2019-08-23 2021-03-01 オシュン株式会社 Water treatment system and water treatment method
JP2021191579A (en) * 2019-08-23 2021-12-16 オシュン株式会社 Water treatment system and water treatment method
JP7217051B2 (en) 2019-08-23 2023-02-02 オシュン株式会社 Water treatment system and water treatment method
CN113864888A (en) * 2020-06-30 2021-12-31 青岛海尔空调器有限总公司 Water tank structure for water washing module, water washing module and air conditioner
CN113864888B (en) * 2020-06-30 2023-04-07 青岛海尔空调器有限总公司 Water tank structure for water washing module, water washing module and air conditioner

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