JP2006218477A - Washing method of wastewater treatment apparatus - Google Patents

Washing method of wastewater treatment apparatus Download PDF

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JP2006218477A
JP2006218477A JP2006020647A JP2006020647A JP2006218477A JP 2006218477 A JP2006218477 A JP 2006218477A JP 2006020647 A JP2006020647 A JP 2006020647A JP 2006020647 A JP2006020647 A JP 2006020647A JP 2006218477 A JP2006218477 A JP 2006218477A
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chamber
purification
purification treatment
purified water
water
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Ryoichi Okamoto
良一 岡本
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Eiwa Kokudo Kankyo Kk
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Eiwa Kokudo Kankyo Kk
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Abstract

<P>PROBLEM TO BE SOLVED: To facilitate washing work by effectively using treated water obtained by treating wastewater by a treatment tank. <P>SOLUTION: This washing method is for the wastewater treatment apparatus having a treatment tank 1 provided with treatment chambers 4-8 treating stepwise wastewater containing sludge components like sanitary sewage discharged from toilets, and a treated water storage tank 2 separately formed from the treatment tank 1 and storing the treated water drawn out of the treatment tank 1. After drawing out wastewater contained in the treatment chambers 4-8 and treated water, the treated water stored in the treated water storage tank 2 is supplied as washing water from the upper part of the most upstream treatment chamber 4 in the treatment tank 1. Thus, sludge components attached to the inner wall of the most upstream treatment chamber 4 are removed, and the treated water is charged to the most upstream treatment chamber 4 and the downstream treatment chambers thereof. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、トイレから排出された屎尿水等からなる排水を迅速かつ高度に浄化処理する排水浄化装置の洗浄方法に関するものである。   The present invention relates to a method for cleaning a wastewater purification apparatus for quickly and highly purifying wastewater composed of manure water or the like discharged from a toilet.

従来、例えば特許文献1に示されるように、カキ殻を接触材として汚水をばっ気処理する第1ばっ気室と、同第1ばっ気室の溢水を多孔質の人工櫨材に接触させて嫌気分解処理を行う嫌気ろ床室と、同嫌気ろ床室で浄化された汚水を流入してカキ殻を接触材としてばっ気処理する第2ばっ気室と、同第2ばっ気室で浄化された水を流入し活性炭に接触させて脱色・脱臭の高度処理を行う仕上げ処理室からなり、しかも汚水を沈殿分離する沈殿分離室と、同沈殿分離された汚水の液体を流入して接触ばっ気する接触ばっ気室と、同接触ばっ気室で接触ばっ気処理した汚水を蓄えて第1ばっ気室に送り込む沈殿室とを第1ばっ気室に流入する汚水の前処理の室として設けた高度処理浄化槽が知られている。
特許第2756657号公報
Conventionally, as shown in, for example, Patent Document 1, a first aeration chamber for aeration treatment of sewage using an oyster shell as a contact material, and an overflow of the first aeration chamber are brought into contact with a porous artificial dredging material. Purified in the anaerobic filter chamber that performs anaerobic decomposition treatment, the second anaerobic chamber that flows in the sewage purified in the anaerobic filter chamber and uses the oyster shell as a contact material, and the second anaerobic chamber The finishing process chamber performs advanced decolorization and deodorization treatment by injecting the collected water into contact with the activated carbon. A pre-treatment chamber for wastewater flowing into the first aeration chamber is provided with a contact aeration chamber to be aired and a sedimentation chamber for storing sewage treated with contact aeration in the contact aeration chamber and sending it to the first aeration chamber Advanced treatment septic tanks are known.
Japanese Patent No. 2756657

上記特許文献1に示されるように、沈殿分離室、接触ばっ気室、第1ばっ気室、嫌気ろ床室、第2ばっ気室および仕上げ処理室が設けられた高度処理浄化槽からなる排水浄化装置によれば、トイレから排出された汚水等からなる排水を段階的に処理することにより、この排水を迅速かつ高度に浄化することができる。しかし、上記排水浄化装置を定期点検する際、またはイベント開催時等において臨時的に設置された排水浄化装置を移転する際等に、上記沈殿分離室および接触ばっ気室等からなる各浄化処理室内の排水を順次導出した後、それぞれ個別に洗浄する必要があるため、その作業が極めて煩雑であるとともに、洗浄作業に要する時間が長くなることが避けられず、上記浄化水の有効利用を図ることが困難であるという問題があった。   As shown in Patent Document 1, waste water purification comprising an advanced treatment septic tank provided with a precipitation separation chamber, a contact aeration chamber, a first aeration chamber, an anaerobic filter floor chamber, a second aeration chamber and a finishing chamber According to the apparatus, this waste water can be purified quickly and highly by treating the waste water composed of sewage discharged from the toilet in stages. However, when regularly checking the waste water purification device or when transferring a waste water purification device temporarily installed at an event, etc., each purification treatment chamber consisting of the precipitation separation chamber and the contact aeration chamber etc. After draining the waste water sequentially, it is necessary to wash each individually, so that the work is extremely complicated and the time required for the washing work is unavoidable, and the above-mentioned purified water is effectively used. There was a problem that was difficult.

本発明は、上記の点に鑑みてなされたものであり、浄化処理槽によって排水を浄化することにより得られた浄化水の有効利用を図ることにより、上記浄化水貯留槽の洗浄作業を容易化できる等の利点を有する排水浄化装置の洗浄方法を提供することを目的としている。   The present invention has been made in view of the above points, and facilitates the cleaning operation of the purified water storage tank by effectively using the purified water obtained by purifying the wastewater by the purification treatment tank. It aims at providing the washing | cleaning method of the waste water purification apparatus which has the advantage of being able to do.

請求項1に係る発明は、トイレから排出された汚水等の汚泥成分を含有する排水を段階的に浄化する複数の浄化処理室を備えた浄化処理槽と、この浄化処理槽とは別体に形成されるとともに、浄化処理槽から導出された浄化水を貯留する浄化水貯留槽とを有する排水浄化装置の洗浄方法であって、上記複数の浄化処理室の内部に収容された排水及び処理水の導出作業を行った後に、上記浄化水貯留槽内に貯留された浄化水を、浄化処理槽の最上流部に位置する最上流浄化処理室の上部から洗浄水として供給することにより、最上流浄化処理室の内壁面に付着した汚泥成分等を除去するとともに、最上流浄化処理室およびその下流側の浄化処理室内に上記浄化水からなる洗浄水を充填するものである。   The invention according to claim 1 is separate from the purification treatment tank provided with a plurality of purification treatment chambers for purifying wastewater containing sludge components such as sewage discharged from the toilet in stages. A wastewater purification apparatus cleaning method comprising a purified water storage tank that is formed and stores purified water derived from a purification treatment tank, wherein the waste water and the treated water are contained in the plurality of purification treatment chambers. After performing the derivation work, the purified water stored in the purified water storage tank is supplied as washing water from the uppermost part of the uppermost stream purification treatment chamber located at the uppermost stream part of the purification treatment tank. In addition to removing sludge components and the like adhering to the inner wall surface of the purification treatment chamber, the uppermost purification treatment chamber and the purification treatment chamber downstream thereof are filled with cleaning water composed of the purified water.

本発明は、上記浄化処理槽によって排水を浄化することにより得られた浄化水を浄化水貯留槽に貯留するとともに、上記浄化水貯留槽を構成する複数の浄化処理室の内部に収容された排水及び処理水の導出作業を行った後に、上記浄化水貯留槽内に貯留された浄化水を、浄化処理槽の最上流部に位置する最上流浄化処理室の上部から洗浄水として供給し、最上流浄化処理室の内壁面に付着した汚泥成分等を除去するとともに、最上流浄化処理室およびその下流側の浄化処理室内に上記浄化水からなる洗浄水を充填するように構成したものであり、これにより上記浄化水貯留槽の洗浄作業を容易化できる等の利点がある。   The present invention stores the purified water obtained by purifying the wastewater by the purification treatment tank in the purified water storage tank, and the wastewater accommodated in the plurality of purification treatment chambers constituting the purified water storage tank. And the treated water derivation operation, the purified water stored in the purified water storage tank is supplied as washing water from the uppermost upstream purification chamber located at the uppermost stream of the purified treatment tank. In addition to removing sludge components and the like adhering to the inner wall surface of the upstream purification treatment chamber, the cleaning water composed of the purified water is filled in the most upstream purification treatment chamber and the purification treatment chamber downstream thereof, Thereby, there exists an advantage that the washing | cleaning operation | work of the said purified water storage tank can be made easy.

図1および図2は、排水浄化装置の具体的構成を示し、この排水浄化装置は、鋼板材、アルミニウム合金材、ステンレス鋼材、プラスチック材、PC(プレストレスコンクリート)材、鉄筋コンクリート材、FRP(繊維強化プラスチック)材またはプラスチック材等からなる浄化処理槽1と、この浄化処理槽1から導出された浄化水を貯留する浄化水貯留槽2と有し、この浄化処理槽1および浄化水貯留槽2が地中に埋設され、あるいは地上に立設された状態で使用されるものである。   FIG. 1 and FIG. 2 show a specific configuration of the waste water purification device, which includes a steel plate material, an aluminum alloy material, a stainless steel material, a plastic material, a PC (prestressed concrete) material, a reinforced concrete material, and an FRP (fiber). A purification treatment tank 1 made of a reinforced plastic material or a plastic material, and a purification water storage tank 2 for storing the purified water derived from the purification treatment tank 1, and the purification treatment tank 1 and the purification water storage tank 2 Is used in a state where it is buried in the ground or standing on the ground.

上記浄化処理槽1は、最上流部に位置する沈殿分離室からなる最上流浄化処理室4と、その下流側に位置する接触ばっ気処理室からなる第1中流浄化処理室5と、その下流側の沈殿室からなる第2中流浄化処理室6と、その下流側の接触濾過室からなる第3中流浄化処理室7と、各浄化処理室4〜8の最下流部に位置する沈殿濾過室からなる最下流浄化処理室8と、この最下流浄化処理室8から導出された処理水を脱色処理して貯留する浄化水貯留室9とを有している。   The purification treatment tank 1 includes an uppermost purification treatment chamber 4 comprising a sedimentation separation chamber located at the most upstream part, a first intermediate flow purification treatment chamber 5 comprising a contact aeration treatment chamber located downstream thereof, and a downstream thereof. The second middle-stream purification treatment chamber 6 composed of a sedimentation chamber on the side, the third middle-stream purification treatment chamber 7 composed of a contact filtration chamber on the downstream side thereof, and the precipitation filtration chamber located in the most downstream portion of each purification treatment chamber 4-8 And a purified water storage chamber 9 for storing the processed water derived from the most downstream purification processing chamber 8 by decolorizing and storing the processed water.

上記最上流浄化処理室(沈殿分離室)4は、図外のトイレから排出管3を介して導出された汚水、または生ゴミをディスポーザにより微粉砕することにより生成された雑排水等の汚泥成分を含有する排水中の紙および粗大異物等の汚泥成分を沈殿させて分離した後に、この分離後の処理水を上記第1中流浄化処理室5にオーバフローさせて導出するとともに、この第1中流浄化処理室5に浮遊物が流失するのをバッフルプレート10により阻止するように構成されている。なお、上記最上流浄化処理室4において沈殿した固形分は、定期的(例えば1年毎)に外部に吸い出されて処理される。   The uppermost stream purification treatment chamber (sediment separation chamber) 4 includes sludge components such as sewage discharged from a toilet (not shown) through a discharge pipe 3 or miscellaneous wastewater generated by finely pulverizing raw garbage with a disposer. The waste water containing paper and sludge components such as coarse foreign matters are precipitated and separated, and the treated water after separation is discharged into the first middle flow purification treatment chamber 5 and discharged. The baffle plate 10 prevents the suspended matter from flowing into the processing chamber 5. The solid content precipitated in the most upstream purification processing chamber 4 is sucked out and processed periodically (for example, every year).

上記第1中流浄化処理室5(接触ばっ気室)には、従来周知のプラスチック製接触材11が充填されるとともに、図外のブロアから供給された空気を放出する散気管12が上記プラスチック製接触材11の下方に配設されている。そして、上記最上流浄化処理室4の上部からオーバフローすることにより第1中流浄化処理室5内に導入された処理水が、散気管12から放出された空気によって撹拌されつつ、上記プラスチック製接触材11に付着して生息した微生物により、上記分離水中の汚泥成分が分解処理されるように構成されている。   The first intermediate flow purification treatment chamber 5 (contact aeration chamber) is filled with a conventionally known plastic contact material 11, and an air diffuser 12 for discharging air supplied from a blower (not shown) is made of the plastic. It is disposed below the contact material 11. Then, the treated water introduced into the first middle flow purification treatment chamber 5 by overflowing from the upper part of the uppermost flow purification treatment chamber 4 is agitated by the air discharged from the air diffuser 12 and the plastic contact material. 11, the sludge components in the separated water are decomposed by microorganisms that have inhabited and inhabited.

また、上記第1中流浄化処理室5と第2中流浄化処理室6との間には、連通路13が下端部に設けられ、第1中流浄化処理室5内において浄化処理された処理水が上記連通路13を介して第2中流浄化処理室6(沈殿室)内に導入されることにより、沈殿処理されることになる。この第2中流浄化処理室6内において沈殿処理された処理水は、導出管14を介して上記第3中流浄化処理室7内にオーバフローすることにより導入される。   In addition, a communication path 13 is provided at the lower end portion between the first middle flow purification treatment chamber 5 and the second middle flow purification treatment chamber 6, and treated water purified in the first middle flow purification treatment chamber 5 By being introduced into the second intermediate flow purification treatment chamber 6 (precipitation chamber) through the communication path 13, the precipitation treatment is performed. The treated water precipitated in the second middle-stream purification treatment chamber 6 is introduced by overflowing into the third middle-stream purification treatment chamber 7 through the outlet pipe 14.

上記第3中流浄化処理室(接触濾過室)7内には、メッシュ状の袋体内にカキ、ホタテ貝、ホッキ貝、真珠貝、アサリ、シジミ、はまぐり、アオヤギ、カラス貝、サザエ、ミル貝もしくは貝化石等からなる貝殻、または死滅して白化した珊瑚が収容されてなる貝殻・珊瑚製接触材15が充填されるとともに、その下方にブロアから供給された空気を放出する散気管16が配設されている。   In the third middle-stream purification treatment chamber (contact filtration chamber) 7, oysters, scallops, sea bream, pearl oysters, clams, clams, clams, blue goats, crows, tuna, mill shells or A shell made of shell fossils or the like, or a shell / smoked contact material 15 containing dead and whitened cocoons are filled, and an air diffuser 16 for releasing the air supplied from the blower is disposed below the shell and smoked contact material 15. Has been.

上記貝殻は、図3に示すように、炭酸カルシウムを主成分とし、かつリン酸カルシウムや炭酸マグネシウム等の微量成分を含有しており、外面側の殻皮層aと、内面側の真珠層bと、その間の角柱層cとからなっている。そして、図4に示すように、上記貝殻の真珠層bが除去された状態で袋体内に収容されることにより上記接触材15が構成されている。   As shown in FIG. 3, the shell includes calcium carbonate as a main component and contains trace components such as calcium phosphate and magnesium carbonate, and includes an outer shell layer a, an inner pearl layer b, And a prismatic layer c. And as shown in FIG. 4, the said contact material 15 is comprised by accommodating in the bag body in the state from which the pearl layer b of the said shell was removed.

上記貝殻の真珠層bを除去する方法としては、適宜の工具を使用して真珠層bを剥離する方法、海岸の波打ち際に貝殻を1年間程度放置して真珠層bを自然浸食させる方法、塩酸等の薬品を使用して真珠層bを溶解させる方法、または多数の貝殻を撹拌機に撹拌して貝殻同士を接触させることにより真珠層bを剥離させる方法等がある。なお、上記自然浸食もしくは撹拌法により真珠層bを除去する場合には、この真珠層bとともに、上記殻皮層aの一部も除去されることになる。   As a method of removing the nacreous layer b of the shell, a method of peeling the nacreous layer b using an appropriate tool, a method of allowing the shell to leave the seashell for about a year at the beach shore, and eroding the nacreous layer b naturally, hydrochloric acid There are a method of dissolving the nacreous layer b using a chemical such as a method, a method of peeling a nacreous layer b by agitating a large number of shells with a stirrer and bringing the shells into contact with each other. When the nacreous layer b is removed by the natural erosion or stirring method, a part of the shell layer a is also removed together with the nacreous layer b.

そして、上記第2中流浄化処理室6から第3中流浄化処理室7内に導入された処理水は、散気管16から放出された空気によって撹拌されつつ、上記貝殻・珊瑚製接触材15に付着した状態で生息する微生物により、上記処理水中の汚泥成分が分解処理される。また、上記第2中流浄化処理室6の下端部からから第3中流浄化処理室7内にオーバフローして導入された処理水は、散気管16から放出された空気によって撹拌されつつ、上記貝殻・珊瑚製接触材15に付着した状態で生息する微生物により、上記処理水中の汚泥成分がさらに分解処理される。   The treated water introduced from the second middle flow purification treatment chamber 6 into the third middle flow purification treatment chamber 7 adheres to the shell / smoked contact material 15 while being agitated by the air released from the air diffuser 16. The sludge components in the treated water are decomposed by the microorganisms that inhabit the state. Further, the treated water introduced by overflowing from the lower end of the second middle flow purification treatment chamber 6 into the third middle flow purification treatment chamber 7 is agitated by the air discharged from the air diffuser 16, and the shell / The sludge components in the treated water are further decomposed by microorganisms that live in a state of adhering to the smoked contact material 15.

上記第3中流浄化処理室7において浄化処理された処理水は、その下端部から最下流浄化処理室8に導出される。この最下流浄化処理室(沈殿濾過室)8は、多孔質体からなるゼオライトが収容された濾過体17を有し、上記第3中流浄化処理室7から導出された処理水中の不純物を沈殿させて汚水と上澄み水とに分離するとともに、この上澄み水中の微細な不純物を上記濾過体17により濾過して浄化水を生成するように構成されている。上記最下流浄化処理室8において生成された浄化水は、上記浄化水貯留室9内にオーバフローして導出される。   The treated water purified in the third middle flow purification treatment chamber 7 is led out to the most downstream purification treatment chamber 8 from its lower end. The most downstream purification treatment chamber (precipitation filtration chamber) 8 has a filter body 17 containing a porous zeolite, and precipitates impurities in the treated water led out from the third intermediate flow purification treatment chamber 7. Thus, the water is separated into sewage and supernatant water, and fine impurities in the supernatant water are filtered by the filter body 17 to generate purified water. The purified water generated in the most downstream purification treatment chamber 8 overflows into the purified water storage chamber 9 and is led out.

また、上記浄化水貯留室9には、図5に示すように、複数の透孔が形成された仕切り板19,20が上下に設置された吸着筒21と、この吸着筒21内の仕切り板19,20間に配設された活性炭収容体22と、浄化水貯留室9内の処理水を吸引して上記活性炭収容体22の下方部に吐出する循環ポンプ23および循環パイプ24を有する循環手段25とが設けられている。上記活性炭収容体22は、布材等からなる袋体内に石炭系の活性炭が充填されることにより構成されている。上記循環手段25により活性炭収容体22の下方部に吐出された処理水が、上記吸着筒21内を通って上記浄化水貯留室9内を循環するとともに、その際に、活性炭収容体22内の石炭系活性炭により色素成分が吸着されて効果的に脱色されるようになっている。   Further, in the purified water storage chamber 9, as shown in FIG. 5, as shown in FIG. 5, an adsorption cylinder 21 in which a plurality of through holes 19 and 20 are vertically installed, and a partition plate in the adsorption cylinder 21. Circulating means having an activated carbon container 22 disposed between 19 and 20 and a circulation pump 23 and a circulation pipe 24 for sucking the treated water in the purified water storage chamber 9 and discharging it to the lower part of the activated carbon container 22. 25. The activated carbon container 22 is configured by filling a bag made of a cloth material or the like with coal-based activated carbon. The treated water discharged to the lower part of the activated carbon container 22 by the circulation means 25 circulates in the purified water storage chamber 9 through the adsorption cylinder 21, and at that time, in the activated carbon container 22 The pigment component is adsorbed by the coal-based activated carbon and effectively decolorized.

上記浄化水貯留室9において脱色処理された浄化水は、図2に示すように、その一部が給水ポンプ26および給水パイプ27を有する給水手段28によってトイレの給水タンク(図示せず)に供給されるとともに、残りが、導出管30を介して上記浄化水貯留槽2に導出されて貯留される。この浄化水貯留槽2は、その容量が最上流浄化処理室4および第1,第2中流浄化処理室5,6の総容量に略等しい値に設定されている。   As shown in FIG. 2, a part of the purified water decolorized in the purified water storage chamber 9 is supplied to a toilet water tank (not shown) by a water supply means 28 having a water supply pump 26 and a water supply pipe 27. In addition, the remainder is led out and stored in the purified water storage tank 2 via the lead-out pipe 30. The capacity of the purified water storage tank 2 is set to a value substantially equal to the total capacity of the most upstream purification process chamber 4 and the first and second intermediate flow purification process chambers 5 and 6.

また、上記給水パイプ27には、必要に応じて浄化水貯留室9内の浄化水を、上記第1,第3中流浄化処理室5,7および最下流浄化処理室8の上部から各浄化処理室5〜8内に洗浄水として供給することにより、各浄化処理室5〜8の内壁面を洗浄するための洗浄パイプ31〜33が連設されている。   Further, the purified water in the purified water storage chamber 9 is supplied to the water supply pipe 27 as needed from the upper portions of the first and third intermediate flow purification treatment chambers 5 and 7 and the most downstream purification treatment chamber 8. Cleaning pipes 31 to 33 for cleaning the inner wall surfaces of the respective purification processing chambers 5 to 8 are connected in series by supplying the chambers 5 to 8 as cleaning water.

上記最上流浄化処理室4と、その下流側に位置する第1,第3中流浄化処理室5,7と、最下流浄化処理室8とは、図2および図6に示すように、浄化処理槽1の側面下部に設置された還流通路35を介して互いに接続されている。そして、上記還流通路35には、この還流通路35を開閉する第1,第2開閉弁36,37が設けられ、上記還流通路35の上流側に位置する第1開閉弁36を開放することにより、上記最上流浄化処理室4と、第1中流浄化処理室5および第2中流浄化処理室6とが連通状態となるように構成されている。また、上記第1開閉弁36を開放状態に維持しつつ、その下流側の第2開閉弁37を開放状態とすることにより、上記最上流浄化処理室4と、第3中流浄化処理室7および最下流浄化処理室8とが連通状態となるように構成されている。   As shown in FIG. 2 and FIG. 6, the most upstream purification treatment chamber 4, the first and third middle-stream purification treatment chambers 5 and 7 and the most downstream purification treatment chamber 8 located on the downstream side thereof are purified. The tanks 1 are connected to each other via a reflux passage 35 installed at the lower side of the tank 1. The recirculation passage 35 is provided with first and second on-off valves 36 and 37 for opening and closing the recirculation passage 35, and the first on-off valve 36 located upstream of the recirculation passage 35 is opened. The uppermost stream purification treatment chamber 4, the first middle flow purification treatment chamber 5, and the second middle flow purification treatment chamber 6 are configured to communicate with each other. Further, by maintaining the first on-off valve 36 in the open state and opening the second on-off valve 37 on the downstream side thereof, the most upstream purification processing chamber 4, the third intermediate flow purification processing chamber 7, The most downstream purification treatment chamber 8 is configured to be in a communication state.

上記最上流浄化処理室4、第1〜第3中流浄化処理室5〜7、最下流浄化処理室8および浄化水貯留室9の上部には、清掃または点検用の開口部40〜43がそれぞれ形成されている。上記最上流浄化処理室4に形成された開口部40は、排水吸引手段の吸引ホースが挿入される吸引口として利用されるものである。また、通常時には、上記開口部40〜43を開閉可能に閉止する閉止蓋(図示せず)が設置されている。さらに、上記排水浄化装置には、浄化水貯留槽2に貯留された浄化水を、洗浄水として最上流浄化処理室4内に供給することにより、この最上流浄化処理室4の内壁面を洗浄するための給水ポンプ45および給水パイプ46を有する浄化水供給手段47が設けられている。   Openings 40 to 43 for cleaning or inspection are provided above the uppermost purification process chamber 4, the first to third intermediate flow purification process chambers 5 to 7, the most downstream purification process chamber 8, and the purified water storage chamber 9, respectively. Is formed. The opening 40 formed in the uppermost stream purification treatment chamber 4 is used as a suction port into which a suction hose of the drainage suction means is inserted. Further, at the normal time, a closing lid (not shown) for closing the openings 40 to 43 so as to be openable and closable is installed. Further, the waste water purification apparatus supplies the purified water stored in the purified water storage tank 2 as cleaning water into the most upstream purification treatment chamber 4 to wash the inner wall surface of the most upstream purification treatment chamber 4. Purified water supply means 47 having a water supply pump 45 and a water supply pipe 46 is provided.

上記構成において、図外のトイレから排出管3を介して最上流浄化処理室(沈殿分離室)4内に導入された排水等は、この最上流浄化処理室4内において紙および粗大異物等の汚泥成分が沈殿分離された後、第1中流処理室(接触ばっ気室)5内に導入される。この第1中流処理室5内に導入された処理水は、その汚泥成分が微生物により分解処理されるとともに、第2中流処理室(沈殿室)に導入されて沈殿処理された後、上記第3中流浄化処理室(接触濾過室)7および最下流浄化処理室(沈殿濾過室)8を経て浄化水貯留室9内に導入されて貯留され、さらに上記浄化水貯留槽2に導出されて貯留される。   In the above-described configuration, wastewater or the like introduced into the uppermost stream purification treatment chamber (precipitation separation chamber) 4 through the discharge pipe 3 from the toilet not shown in the figure is not limited to paper, coarse foreign matters, etc. in the uppermost stream purification treatment chamber 4. After the sludge component is precipitated and separated, it is introduced into the first middle flow treatment chamber (contact aeration chamber) 5. The treated water introduced into the first middle-stream treatment chamber 5 is decomposed by microorganisms and the sludge components are introduced into the second middle-stream treatment chamber (sedimentation chamber) and subjected to precipitation treatment, and then the third It is introduced and stored in the purified water storage chamber 9 via the middle-stream purification treatment chamber (contact filtration chamber) 7 and the most downstream purification treatment chamber (precipitation filtration chamber) 8, and is further led out and stored in the purified water storage tank 2. The

そして、野外演奏会等のイベント開催時または災害の発生時等に、所定個所に一時的に設置された上記排水浄化装置を撤去する際、または公園等において定常的に設置された公衆トイレ用の排水浄化装置を定期点検する際または補修する際等には、バキュームカー等に設けられた排水吸引手段の吸引ホースを、最上流浄化処理室4の開口部40に挿入し、その内部の排水を吸引して外部に導出する。また、上記還流通路35に設けられた第1,第2開閉弁(開閉手段)36,37を順次開放した状態で、最上流浄化処理室4内に導入された処理水を吸引して外部に導出する作業を継続することにより、第1〜第3中流浄化処理室5〜7および最下流浄化処理室8内から上記還流通路35を介して最上流浄化処理室4内に還流された処理水を順次外部に導出しつつ、上記浄化水供給手段47から供給される洗浄水により最上流浄化処理室4の内壁面に付着した汚泥成分等を除去するとともに、最上流浄化処理室4および第1,第2中流浄化処理室5,6内に上記浄化水からなる洗浄水を充填し、この洗浄水を利用して上記各浄化処理室4〜6の内壁面を洗浄する。   And for events such as outdoor concerts or when disasters occur, when removing the waste water purification equipment temporarily installed at a predetermined location, or for public toilets installed regularly in parks, etc. When regularly checking or repairing the waste water purification device, the suction hose of the waste water suction means provided in the vacuum car or the like is inserted into the opening 40 of the most upstream purification treatment chamber 4 to drain the internal waste water. Suction and lead out. Further, with the first and second on-off valves (opening / closing means) 36 and 37 provided in the reflux passage 35 being opened sequentially, the treated water introduced into the most upstream purification treatment chamber 4 is sucked to the outside. By continuing the work to be led out, the treated water recirculated from the first to third middle flow purification treatment chambers 5 to 7 and the most downstream purification treatment chamber 8 into the most upstream purification treatment chamber 4 through the return passage 35. In addition to removing the sludge components and the like adhering to the inner wall surface of the uppermost stream purification treatment chamber 4 with the washing water supplied from the purified water supply means 47, the uppermost purification treatment chamber 4 and the first The second intermediate flow purification treatment chambers 5 and 6 are filled with the washing water made of the purification water, and the inner wall surfaces of the purification treatment chambers 4 to 6 are washed using the washing water.

このようにして各浄化処理室4〜8の上端部に形成された開口部40〜43に上記吸引ホースを順番に挿入してそれぞれ個別に内部の排水または処理水を外部に導出する等の繁雑な作業を要することなく、各浄化処理室4〜8の内部を迅速かつ容易に空にした状態で、野外演奏会等のイベント開催時または災害の発生時等に設置された上記排水浄化装置を撤去する作業、または公園等において定常的に設置された公衆トイレ用の排水浄化装置を定期点検する作業および補修する作業等を容易かつ適正に行うことが可能となる。   In this way, the suction hoses are sequentially inserted into the openings 40 to 43 formed at the upper end portions of the respective purification treatment chambers 4 to 8, and the internal waste water or the treated water is individually led out to the outside. The waste water purification device installed at the time of events such as outdoor concerts or when disasters occur, etc., with the interior of each of the purification treatment chambers 4 to 8 being emptied quickly and easily without requiring a tedious work It is possible to easily and appropriately perform the work of removing, the work of regularly inspecting and repairing the drainage purification apparatus for public toilets regularly installed in a park or the like.

上記のように構成された排水浄化装置は、トイレから排出された排水を段階的に浄化する複数の浄化処理室4〜8および浄化処理された浄化水を貯留する浄化水貯留室9を備えた浄化処理槽1と、この浄化処理槽1とは別体に形成されるとともに、浄化水処理槽1の浄化水貯留室9から導出された浄化水を貯留する浄化水貯留槽2とを備えているため、トイレから排出管3を介して導出された排水中の紙および粗大異物等の汚泥成分を最上流浄化処理室4において沈殿分離室後に、この最上流浄化処理室4から第1〜第3中流浄化処理室5〜7および最下流浄化処理室8に順次導出された処理水中の汚泥成分を微生物の作用等により段階的に浄化した状態で、この浄化水を上記浄化水貯留室9および浄化水貯留槽2内に導出して貯留し、給水手段28によってトイレの給水タンクに供給する等により、有効に利用することが可能となる。   The waste water purification apparatus configured as described above includes a plurality of purification treatment chambers 4 to 8 that purify the waste water discharged from the toilet in stages, and a purified water storage chamber 9 that stores the purified water that has been purified. A purification treatment tank 1 and a purification water storage tank 2 that is formed separately from the purification treatment tank 1 and stores purified water derived from the purification water storage chamber 9 of the purification water treatment tank 1 are provided. Therefore, the paper and the sludge components such as coarse foreign matters led out from the toilet through the discharge pipe 3 are separated from the first upstream purification processing chamber 4 after the precipitation separation chamber in the uppermost upstream purification processing chamber 4. 3 In a state where the sludge components in the treated water sequentially led to the middle-stream purification treatment chambers 5 to 7 and the most downstream purification treatment chamber 8 are purified stepwise by the action of microorganisms, the purified water is supplied to the purified water storage chamber 9 and Derived and stored in the purified water storage tank 2 for water supply By such supply to the water supply tank toilet by the step 28, it is possible to effectively use.

そして、上記浄化水貯留槽2の容量を、最上流部に位置する沈殿分離室からなる最上流浄化処理室4、その下流側に位置する接触ばっ気処理槽からなる第1中流浄化処理室5およびその下流側の沈殿室からなる第2中流浄化処理室6の総容量に略等しい値に設定したため、上記のように排水浄化装置を定期点検作業および補修作業を行う際等において、各浄化処理室4〜8の内部に収容された排水および処理水を順次外部に導出した後に、浄化水貯留槽2内の浄化水を最上流浄化処理室4および第1,第2中流浄化処理室5,6内を浄化水で満たして適正に洗浄できるという利点がある。   And the capacity | capacitance of the said purified water storage tank 2 is made into the 1st middle flow purification process chamber 5 which consists of the uppermost stream purification process chamber 4 which consists of a sedimentation separation chamber located in the most upstream part, and the contact aeration process tank located in the downstream. In addition, since the total capacity of the second middle-stream purification treatment chamber 6 composed of the sedimentation chamber on the downstream side is set to a value approximately equal to the total capacity, each purification treatment is performed when the drainage purification apparatus is regularly inspected and repaired as described above. After the waste water and the treated water accommodated in the chambers 4 to 8 are sequentially led out to the outside, the purified water in the purified water storage tank 2 is supplied to the most upstream purification treatment chamber 4 and the first and second intermediate flow purification treatment chambers 5, 5. There is an advantage that the inside of 6 can be properly cleaned by filling with purified water.

特に、上記実施形態では、上記排水浄化装置の最上流部に位置する最上流浄化処理室4に、排水を吸引するための開口部(吸引口)40を設けるとともに、上記最上流浄化処理室4の下流側に配設された第1〜第3中流浄化処理室5〜7および最下流浄化処理室8内の処理水を最上流浄化処理室内に還流させる還流通路35を有する還流手段と、上記浄化水貯留槽2内に貯留された浄化水を最上流浄化処理室4内に供給する浄化水供給手段47とを設けたため、バキュームカー等に設けられた排水吸引手段の吸引ホースを、最上流浄化処理室4の開口部40に挿入して、その内部の排水を吸引することにより、その内壁面を洗浄することができる。   In particular, in the above-described embodiment, the most upstream purification treatment chamber 4 located at the most upstream portion of the waste water purification apparatus is provided with an opening (suction port) 40 for sucking waste water, and the most upstream purification treatment chamber 4. A reflux means having a reflux passage 35 for refluxing treated water in the first to third intermediate flow purification treatment chambers 5 to 7 and the most downstream purification treatment chamber 8 disposed on the downstream side of the uppermost flow purification treatment chamber; Since the purified water supply means 47 for supplying the purified water stored in the purified water storage tank 2 to the uppermost stream purification treatment chamber 4 is provided, the suction hose of the drainage suction means provided in the vacuum car or the like is connected to the uppermost stream. The inner wall surface can be cleaned by inserting it into the opening 40 of the purification treatment chamber 4 and sucking the waste water inside.

すなわち、上記排水吸引手段により最上流浄化処理室4内に収容された排水を外部に導出した後に、上記還流通路35に設けられた第1,第2開閉弁(開閉手段)36,37を順次開放した状態で、最上流浄化処理室4内に導入された処理水を吸引して外部に導出する作業を継続することにより、第1〜第3中流浄化処理室5〜7および最下流浄化処理室8内から上記還流通路35を介して最上流浄化処理室4内に還流された処理水を順次外部に導出することができる。そして、上記浄化水供給手段47から供給される洗浄水によって最上流浄化処理室4の内壁面に付着した汚泥成分等を除去するとともに、最上流浄化処理室4および第1,第2中流浄化処理室5,6内に上記浄化水からなる洗浄水を充填することができる。したがって、各浄化処理室4〜8の上端部に形成された開口部40〜43に上記吸引ホースを順番に挿入してそれぞれ個別に内部の排水または処理水を外部に導出する等の繁雑な作業を要することなく、各浄化処理室4〜8の内部を迅速かつ容易に空にすることができる。   That is, after the waste water accommodated in the most upstream purification processing chamber 4 is led out to the outside by the waste water suction means, the first and second on-off valves (open / close means) 36 and 37 provided in the reflux passage 35 are sequentially provided. In the opened state, the first to third middle-stream purification treatment chambers 5 to 7 and the most downstream purification treatment are carried out by continuing the work of sucking the treated water introduced into the most upstream purification treatment chamber 4 and leading it to the outside. The treated water refluxed from the chamber 8 through the reflux passage 35 into the most upstream purification treatment chamber 4 can be sequentially led out. And while removing the sludge component etc. which adhered to the inner wall surface of the most upstream purification process chamber 4 with the wash water supplied from the said purified water supply means 47, the most upstream purification process chamber 4 and the 1st, 2nd middle flow purification process. The chambers 5 and 6 can be filled with cleaning water composed of the purified water. Therefore, complicated work such as inserting the suction hoses into the openings 40 to 43 formed at the upper ends of the respective purification treatment chambers 4 to 8 in order and individually leading the internal drainage or treated water to the outside. Therefore, the inside of each of the purification treatment chambers 4 to 8 can be emptied quickly and easily.

また、上記実施形態では、浄化処理槽1の浄化水貯留室9内に貯留された浄化水を、第1,第3中流浄化処理室5,7および最下流浄化処理室8の上部から洗浄水としてそれぞれ供給する洗浄パイプ31〜33を備えた上記給水手段28からなる浄化水供給手段を設けたため、上記第1〜第3中流浄化処理室5〜7および最下流浄化処理室8内の処理水を最上流浄化処理室4内に還流させて順次外部に導出させる際に、上記各浄化処理室5〜8の内壁面に付着した汚泥成分等を、上記浄化水供給手段から供給される洗浄水により効果的に除去することができるという利点がある。   Further, in the above embodiment, the purified water stored in the purified water storage chamber 9 of the purification treatment tank 1 is washed from the upper portions of the first and third intermediate flow purification treatment chambers 5 and 7 and the most downstream purification treatment chamber 8. As the purified water supply means comprising the water supply means 28 provided with the cleaning pipes 31 to 33 respectively supplied as above, the treated water in the first to third intermediate flow purification treatment chambers 5 to 7 and the most downstream purification treatment chamber 8 is provided. Is returned to the uppermost purification process chamber 4 and sequentially led out to the outside, and the sludge components adhering to the inner wall surfaces of the respective purification process chambers 5 to 8 are washed water supplied from the purified water supply means. There is an advantage that it can be effectively removed.

さらに、上記実施形態では、排水浄化装置の第3中流浄化処理室7内に充填される貝殻・珊瑚接触材15として、少なくとも内面側の真珠層bが除去されて多孔質の角柱層cが露出したカキ殻等を使用したため、この貝殻・珊瑚接触材15と、上記第3中流浄化処理室7内に導入された処理水中の汚泥成分を分解処理する微生物との親和性を高めて、これらを好適に繁殖させることができる。したがって、上記多孔質の角柱層cにおいて繁殖した微生物により、処理水中の汚泥成分を効果的に分解処理して排水を効率よく浄化することができる。しかも、上記排水浄化装置の設置当初から、上記微生物の分解処理機能等を発揮させることができるため、上記排水浄化装置により浄化処理された浄化水を外部に放出した場合に、環境汚染が発生するのを効果的に防止することができるとともに、上記浄化水をトイレの洗浄水として利用することにより、水資源の有効利用を図ることができるという利点がある。   Furthermore, in the above embodiment, as the shell / shell contact material 15 filled in the third middle-stream purification treatment chamber 7 of the waste water purification apparatus, at least the inner pearl layer b is removed and the porous prismatic layer c is exposed. Since the oyster shells and the like were used, the affinity between the shell / shell contact material 15 and the microorganisms for decomposing the sludge components in the treated water introduced into the third middle flow purification treatment chamber 7 is increased. It can be suitably propagated. Therefore, the microorganisms propagated in the porous prismatic layer c can effectively decompose the sludge components in the treated water and efficiently purify the waste water. In addition, since the microbial decomposition treatment function and the like can be exerted from the beginning of the installation of the waste water purification device, environmental pollution occurs when the purified water purified by the waste water purification device is discharged to the outside. In addition to being able to effectively prevent this, there is an advantage that effective use of water resources can be achieved by using the purified water as toilet wash water.

また、上記第1中流浄化処理室5および第3中流浄化処理室7において排水がばっ気処理されることにより、処理水が酸性化した場合には、上記貝殻・珊瑚から炭酸カルシウム(CaCO)を迅速に溶解させて、上記処理水を中和することができる。すなわち、上記真珠層bが除去された貝殻は、その溶解が進行し易いという特性を有しているため、酸性化した処理水を効果的に中性化できるという利点がある。 In addition, when the wastewater is aerated in the first middle flow purification treatment chamber 5 and the third middle flow purification treatment chamber 7 and the treated water is acidified, calcium carbonate (CaCO 2 ) is produced from the shells and shells. Can be dissolved quickly to neutralize the treated water. That is, since the shell from which the nacreous layer b has been removed has a characteristic that its dissolution is easy to proceed, there is an advantage that the acidified treated water can be effectively neutralized.

しかも、上記のように第3中流浄化処理室7において処理水が中性化されるので、太陽虫等の原生動物および腔腸動物を多量に発生、繁殖させることができる。このため、上記処理水中に存在する大腸菌等の細菌を、上記原生動物等に補食させて絶滅させることにより、上記排水浄化処装置から導出される浄化処理水中に細菌が混入するのを効果的に防止することができる。   Moreover, since the treated water is neutralized in the third middle-stream purification treatment chamber 7 as described above, a large amount of protozoa such as solar insects and coelenterates can be generated and propagated. For this reason, bacteria such as Escherichia coli present in the treated water are effectively fed into the clarified treated water derived from the wastewater purification treatment device by feeding on the protozoa and extinguishing the bacteria. Can be prevented.

さらに、上記処理水にリン成分が含有されている場合には、下式に示すように、上記炭酸カルシウムから遊離したCaイオンと、処理水中のリンイオン(HPO)とを効果的に反応させることにより、処理水を迅速に中性化してリン酸カルシウム(Ca(OH)(PO)を生成することができる。そして、上記リン酸カルシウム(Ca(OH)(PO)を、浄化水貯留室9に配設された上記活性炭収容体22中の活性炭に吸着させて回収することにより、これを肥料等として使用可能であるという利点がある。 Further, when the treated water contains a phosphorus component, as shown in the following formula, Ca ions liberated from the calcium carbonate and phosphorus ions (HPO 4 ) in the treated water are effectively reacted. Thus, the treated water can be quickly neutralized to produce calcium phosphate (Ca (OH) (PO 4 ) 3 ). Then, the calcium phosphate (Ca (OH) (PO 4 ) 3 ) is used as a fertilizer by adsorbing and recovering the calcium phosphate (Ca (OH) (PO 4 ) 3 ) on the activated carbon in the activated carbon container 22 disposed in the purified water storage chamber 9. There is an advantage that it is possible.

5Ca+3HPO → Ca(OH)(PO+3H
なお、上記処理水中のリン酸カルシウム(Ca(OH)(PO)は、その一部が最下流浄化処理室8内において沈殿するとともに濾過体17により吸着され、その残りが上記活性炭吸着室22内において活性炭に吸着されることとなる。上記処理水中に残存する微量のリン成分を除去するためには、上記活性炭吸着室22内に、カキ殻等の貝殻が充填されたリン吸着筒を配設した構造とすることが望ましい。
5Ca + 3HPO 4 → Ca (OH) (PO 4 ) 3 + 3H 2 O
A part of the calcium phosphate (Ca (OH) (PO 4 ) 3 ) in the treated water is precipitated in the most downstream purification treatment chamber 8 and is adsorbed by the filter body 17, and the rest is the activated carbon adsorption chamber 22. It will be adsorbed by the activated carbon. In order to remove a small amount of phosphorus component remaining in the treated water, it is desirable to have a structure in which a phosphorus adsorption cylinder filled with shells such as oyster shells is disposed in the activated carbon adsorption chamber 22.

また、上記実施形態では、図5に示すような循環手段25を設け、浄化水貯留室9内の処理水を吸引して上記活性炭収容体22の下方部に吐出することにより、上記浄化水貯留室9内に処理水を循環させるように構成したため、上記処理水中の色素成分を、活性炭収容体22内に収容された石炭系活性炭により効果的に吸着して脱色作用を向上させることができるという利点がある。   Moreover, in the said embodiment, the circulating means 25 as shown in FIG. 5 is provided, the said purified water storage is carried out by attracting | sucking the treated water in the purified water storage chamber 9, and discharging it to the lower part of the said activated carbon container 22. FIG. Since the treatment water is circulated in the chamber 9, the pigment component in the treatment water can be effectively adsorbed by the coal-based activated carbon accommodated in the activated carbon container 22 to improve the decolorization action. There are advantages.

さらに、上記実施形態では、第3中流浄化処理室7の上流側にプラスチック製接触材11が充填された第1中流浄化処理室5と、この第1中流浄化処理室5において処理された処理水中の不純物等を沈殿させる沈殿室からなる第2中流浄化処理室6を配設し、排水をある程度浄化した状態で、第3中流浄化処理室7に供給するように構成したため、この第3中流浄化処理室7内に配設されたカキ殻等の貝殻が早期に汚損されたり、貝殻が溶解して消失したりするのを効果的に抑制できるという利点がある。   Furthermore, in the above embodiment, the first middle-stream purification treatment chamber 5 in which the plastic contact material 11 is filled on the upstream side of the third middle-stream purification treatment chamber 7 and the treated water treated in the first middle-stream purification treatment chamber 5. Since the second middle-stream purification treatment chamber 6 comprising a sedimentation chamber for precipitating impurities and the like is disposed so that the waste water is purified to some extent, the third middle-stream purification treatment chamber 7 is supplied. There is an advantage that it is possible to effectively suppress the shells such as oyster shells disposed in the processing chamber 7 from being polluted at an early stage or from being dissolved and lost.

また、上記浄化水貯留槽2内に貯留された浄化水を最上流浄化処理室4内に供給する浄化水供給手段47を設けるとともに、上記浄化水貯留室9内に貯留された浄化水を第1,第3中流浄化処理室5,7および最下流浄化処理室8内に洗浄水として供給する洗浄パイプ31〜33を有する給水手段28を設けてなる上記実施形態に代え、浄化水貯留室9内に貯留された浄化水を最上流浄化処理室4内に供給する浄化水供給手段と、上記浄化水貯留槽2内に貯留された浄化水を第1,第3中流浄化処理室5,7および最下流浄化処理室8等内に供給する浄化水供給手段とを設けた構造としてもよい。   In addition, a purified water supply means 47 is provided for supplying purified water stored in the purified water storage tank 2 into the most upstream purification processing chamber 4, and purified water stored in the purified water storage chamber 9 is supplied to Instead of the above-described embodiment in which the water supply means 28 having the cleaning pipes 31 to 33 to be supplied as cleaning water is provided in the first middle flow purification processing chambers 5, 7 and the most downstream purification processing chamber 8, the purified water storage chamber 9 Purified water supply means for supplying the purified water stored in the uppermost purification process chamber 4 and purified water stored in the purified water storage tank 2 to the first and third intermediate flow purification process chambers 5, 7. And it is good also as a structure which provided the purified water supply means supplied in the most downstream purification processing chamber 8 grade | etc.,.

さらに、上記第1,第3中流浄化処理室5,7内の処理水を最上流浄化処理室4内に還流させる還流通路35を有する還流手段に代え、処理水移送ポンプまたはエアリフト(圧縮間空気を用いた移送手段)を設けることにより、上記処理水を強制的に最上流浄化処理室4内に還流させるようにしてもよい。   Further, instead of the recirculation means having a recirculation passage 35 for recirculating the treated water in the first and third intermediate flow purification treatment chambers 5 and 7 into the uppermost flow purification treatment chamber 4, a treated water transfer pump or an air lift (compressed air) The treated water may be forcibly recirculated into the uppermost stream purification treatment chamber 4 by providing a transfer means using

また、図7に示すように、上記浄化水貯留室9内に貯留された浄化水を吸引する第1吸引パイプ51と、浄化水貯留槽2内に貯留された浄化水を吸引する第2吸引パイプ52と、両吸引パイプ51,52の合流部よりも上流側に配設された給水ポンプ53と、各浄化処理室4〜8内に洗浄水を供給する洗浄パイプ54〜57とを有する浄化水供給手段58を設け、上記両吸引パイプ51,52に設けられた開閉弁59,60の一方を閉止するとともに他方を開放した状態で、上記給水ポンプ53を作動させることにより、上記浄化水貯留室9または浄化水貯留槽2内の浄化水を吸引して上記各浄化処理室4〜8内に選択的に供給することにより、各浄化処理室4〜8の内壁面に付着した汚泥成分等を順次除去するように構成してもよい。   Further, as shown in FIG. 7, a first suction pipe 51 that sucks purified water stored in the purified water storage chamber 9 and a second suction that sucks purified water stored in the purified water storage tank 2. Purification having a pipe 52, a water supply pump 53 disposed on the upstream side of the joining portion of both suction pipes 51, 52, and washing pipes 54-57 for supplying washing water into the respective purification treatment chambers 4-8. The water supply means 58 is provided, and the water supply pump 53 is operated in a state where one of the on-off valves 59 and 60 provided in the suction pipes 51 and 52 is closed and the other is opened. The sludge components adhering to the inner wall surfaces of the respective purification treatment chambers 4 to 8 by sucking the purified water in the chamber 9 or the purified water storage tank 2 and selectively supplying them into the respective purification treatment chambers 4 to 8 May be sequentially removed.

さらに、浄化処理槽1の最下流部に設けられた浄化水貯留室9内に、図8に示すように、複数の活性炭収容体22a〜22cを設置するとともに、循環ポンプ23から吐出された処理水を各活性炭収容体22a〜22cの下方部にそれぞれ吐出させる分岐管24a〜24cを設け、この分岐管24a〜24cの上流部に位置する循環パイプ24に設けられた圧力計61の検出圧力に応じて各分岐管24a〜24cに設けられた自動開閉弁62a〜62cを開閉制御することにより、使用する活性炭収容体22a〜22cを順次切り換えるように構成してもよい。   Furthermore, in the purified water storage chamber 9 provided in the most downstream part of the purification treatment tank 1, as shown in FIG. 8, a plurality of activated carbon containers 22a to 22c are installed, and the treatment discharged from the circulation pump 23 Branch pipes 24a to 24c for discharging water to the lower portions of the respective activated carbon containers 22a to 22c are provided, and the detected pressure of the pressure gauge 61 provided on the circulation pipe 24 located upstream of the branch pipes 24a to 24c is set. Accordingly, the activated carbon containers 22a to 22c to be used may be sequentially switched by controlling the automatic opening and closing valves 62a to 62c provided in the branch pipes 24a to 24c.

すなわち、上記分岐管24aに設けられた自動開閉弁62aを開放するとともに、他の自動開閉弁62b,62cを閉止した状態で、上記循環ポンプ23を作動させることにより、上記圧力計61により処理水の供給圧力を検出しつつ、第1の活性炭収容体22aに処理水を供給する。この第1の活性炭収容体22aに目詰まりが生じる等により、その処理能力が低下すると、上記圧力計61の検出圧力が上昇するため、これに対応して上記自動開閉弁62a〜62cの開閉制御を実行することにより、使用する活性炭収容体22a〜22cを順次切り換えるようにする。このように構成することにより、各活性炭収容体22a〜22cの使用時期および頻度を適正に設定してランニングコストを低下させることができるという利点がある。   That is, while the automatic open / close valve 62a provided in the branch pipe 24a is opened and the other automatic open / close valves 62b and 62c are closed, the circulating pump 23 is operated, whereby the pressure gauge 61 is used to treat the treated water. , The treated water is supplied to the first activated carbon container 22a. If the processing capacity of the first activated carbon container 22a is reduced due to clogging or the like, the pressure detected by the pressure gauge 61 is increased. Accordingly, the opening / closing control of the automatic opening / closing valves 62a to 62c is accordingly performed. By executing this, the activated carbon containers 22a to 22c to be used are sequentially switched. By comprising in this way, there exists an advantage that a running cost can be reduced by setting appropriately the use time and frequency of each activated carbon container 22a-22c.

なお、上記浄化水貯留室9内に複数の活性炭収容体22a〜22cを設置するとともに、図9に示すように、各活性炭収容体22a〜22cの下方部にそれぞれ処理水を供給して循環させる複数の循環ポンプ23a〜23cおよび循環パイプ24a〜24cを有する循環手段25a〜25cを個別に設けた構造としてもよく、あるいは容量の大きな単一の循環ポンプ(図示せず)により、各活性炭収容体22a〜22cの下方部に対して同時に処理水を供給するように構成してもよい。   In addition, while installing the some activated carbon container 22a-22c in the said purified water storage chamber 9, as shown in FIG. 9, it supplies and circulates treated water to the lower part of each activated carbon container 22a-22c, respectively. It is good also as a structure which provided separately the circulation means 25a-25c which has the some circulation pumps 23a-23c and the circulation pipes 24a-24c, or each activated carbon container by a single circulation pump (not shown) with a big capacity | capacitance. You may comprise so that treated water may be simultaneously supplied with respect to the lower part of 22a-22c.

また、図10に示すように、浄化水貯留槽2内に貯留された浄化水の異常、つまり浄化水貯留槽2内に貯留された浄化水の量が基準値以上となってこの貯留槽2が満杯になり、または貯留された浄化水の水質が低下してph、色度(濁度)、残留塩素濃度の何れかが基準値よりも悪化する等の異常が発生したか否かを検出する異常検出手段63と、この異常検出手段63において異常が検出された場合に異常検出信号を管理部64に送信する送信手段65を設けた構造としてもよい。このように構成した場合には、上記浄化処理槽1に設けられた各浄化処理室4〜8による排水の浄化機能が低下し、あるいは多量の排水が一時に排水処理槽1に導入される等により、各浄化処理室4〜8による排水の浄化機能が不足した状態にあるために、点検作業および補修作業等が必要であることを管理者に対して適正に認識させることができる。   Further, as shown in FIG. 10, the abnormality of the purified water stored in the purified water storage tank 2, that is, the amount of the purified water stored in the purified water storage tank 2 becomes equal to or greater than a reference value. Detects whether abnormalities such as ph, chromaticity (turbidity), and residual chlorine concentration have deteriorated below the standard value due to the water being full or the quality of the stored purified water being reduced It is also possible to provide a structure provided with an abnormality detection means 63 for transmitting and a transmission means 65 for transmitting an abnormality detection signal to the management unit 64 when an abnormality is detected in the abnormality detection means 63. When configured in this way, the purification function of the waste water by the purification treatment chambers 4 to 8 provided in the purification treatment tank 1 is reduced, or a large amount of waste water is introduced into the waste water treatment tank 1 at a time, etc. Thus, since the purification function of the waste water by each of the purification treatment chambers 4 to 8 is in a state of being insufficient, it is possible to appropriately recognize the administrator that the inspection work, the repair work, and the like are necessary.

また、図11に示すように、浄化処理槽1の最上流浄化処理室4と並列に排水貯留槽66を設けるとともに、上記最上流浄化処理室4内に収容された排水を排水貯留槽66内に移送する移送ポンプ67および移送管68を備えた移送手段69を設けることにより、必要に応じて最上流浄化処理室4内の排水を排水貯留槽66内に移送するように構成してもよい。   As shown in FIG. 11, a drainage storage tank 66 is provided in parallel with the uppermost purification process chamber 4 of the purification process tank 1, and the wastewater stored in the uppermost purification process chamber 4 is disposed in the drainage storage tank 66. By providing a transfer means 69 provided with a transfer pump 67 and a transfer pipe 68 for transferring the waste water in the uppermost stream purification treatment chamber 4 to the waste water storage tank 66 as necessary. .

例えば、上記浄化水貯留槽2内に貯留された浄化水の異常を検出する異常検出手段63の検出信号に応じ、浄化水貯留槽2内が浄化水で満杯になり、あるいは最上流浄化処理室4内に大量の排水が流入して上記浄化水の水質が低下する等の異常が発生したことが検出された場合に、制御手段48から上記移送ポンプ67作動指令信号を出力してこの移送ポンプ67を作動させることにより、最上流浄化処理室4内の排水を排水貯留槽66内に移送した後、制御手段48から浄化水供給手段45の給水ポンプ46に作動指令信号を出力してこの給水ポンプ46を作動させることにより、浄化水貯留槽2内の浄化水を浄化処理槽1の最上流浄化処理室4等の内部に供給するように構成してもよい。なお、図10および図11において、47aは、浄化水供給手段47により浄化処理室4〜6に供給される浄化水の供給方向を切り換える三方切換弁である。   For example, the inside of the purified water storage tank 2 is filled with purified water in accordance with the detection signal of the abnormality detection means 63 that detects an abnormality of the purified water stored in the purified water storage tank 2, or the most upstream purification processing chamber. 4, when it is detected that an abnormality has occurred such as a large amount of wastewater flowing in and the quality of the purified water is lowered, the transfer pump 67 operation command signal is output from the control means 48 to By operating 67, the waste water in the most upstream purification treatment chamber 4 is transferred into the waste water storage tank 66, and then an operation command signal is output from the control means 48 to the water supply pump 46 of the purified water supply means 45. You may comprise so that the purified water in the purified water storage tank 2 may be supplied to the inside of the uppermost purification process chamber 4 etc. of the purified treatment tank 1 by operating the pump 46. 10 and 11, 47 a is a three-way switching valve that switches the supply direction of the purified water supplied to the purification treatment chambers 4 to 6 by the purified water supply means 47.

上記のように構成した場合には、排水を吸引して外部に導出する作業の2回分を同時に行うことができるため、上記浄化処理槽1の点検作業および補修作業等を行う周期を約2倍に延ばすことができるという利点がある。なお、上記移送ポンプ67により最上流浄化処理室4内の排水を排水貯留槽66内に強制的に移送するようにした上記実施形態に代え、最上流浄化処理室4内の排水をオーバフローさせることにより、上記排水貯留槽66内に上記排水を移送させるように構成してもよい。   In the case of the configuration described above, since the work of sucking out the waste water and leading it out to the outside can be performed at the same time, the period of performing the inspection work and the repair work of the purification tank 1 is approximately doubled. There is an advantage that it can be extended. Instead of the embodiment in which the transfer pump 67 forcibly transfers the wastewater in the uppermost purification treatment chamber 4 into the wastewater storage tank 66, the wastewater in the uppermost purification treatment chamber 4 is allowed to overflow. Thus, the waste water may be transferred into the waste water storage tank 66.

また、図12に示すように、トイレから排出された汚水、または生ゴミをディスポーザにより微粉砕することによりされた生成された雑排水等の汚泥成分を含有する排水を段階的に浄化する複数の浄化処理室4〜8と、その最下流部に位置する最下流浄化処理室8から導出された浄化水を貯留する浄化水貯留室9を有する浄化処理槽1と、この浄化水処理槽1の最下流部に連設された浄化水貯留槽2と、上記浄化水処理槽1の最上流部に位置する最上流浄化処理室4と並列に設置された汚泥処理槽70と、上記最上流浄化処理室4内に収容された排水を汚泥分解槽に移送する移送管等からなる移送手段71とを備え、この移送手段71を介して上記汚泥分解槽70に移送された排水中の汚泥成分を嫌気分解処理する嫌気分解室72と、この嫌気分解室72から導出された処理水を好気分解処理する好気分解室73と、この好気分解室73から導出された処理水を沈殿分離処理する沈殿分離室74とを上記汚泥分解槽70に設けた構造としてもよい。   In addition, as shown in FIG. 12, a plurality of wastewater containing sludge components such as sewage discharged from a toilet or generated wastewater generated by pulverizing raw garbage with a disposer are gradually purified. A purification treatment tank 1 having a purification treatment chamber 4 to 8 and a purification water storage chamber 9 for storing the purified water derived from the most downstream purification treatment chamber 8 located at the most downstream portion of the purification treatment chamber 1. The purified water storage tank 2 connected to the most downstream portion, the sludge treatment tank 70 installed in parallel with the most upstream purification treatment chamber 4 located at the most upstream part of the purified water treatment tank 1, and the most upstream purification Transfer means 71 comprising a transfer pipe or the like for transferring the wastewater stored in the processing chamber 4 to the sludge decomposition tank, and the sludge components in the wastewater transferred to the sludge decomposition tank 70 via the transfer means 71. An anaerobic decomposition chamber 72 for anaerobic decomposition treatment, The sludge decomposition tank 70 includes an aerobic decomposition chamber 73 for aerobically decomposing treated water derived from the decomposition chamber 72 and a precipitation separation chamber 74 for performing precipitation separation treatment on the treated water derived from the aerobic decomposition chamber 73. It is good also as a structure provided in.

上記嫌気分解室72には、移送手段71を介して最上流浄化処理室4内からオーバフローまたは強制的に移送された排水中の汚泥成分を構成する有機物を嫌気条件下で分解してメタンガスを生成するメタン菌が収容されている。また、上記好気分解室73には、嫌気分解室72から導出された処理水中の残存有機成分の分解およびアンモニアの硝化等を行う好気性生物が収容されている。そして、上記好気生分解室73により分解処理されて沈殿分離室74に導出された処理水は、この沈殿部隣室74内において沈殿処理された後、散水または放水され、あるいは防火水等として再利用される。   In the anaerobic decomposition chamber 72, methane gas is generated by decomposing organic substances constituting sludge components in the wastewater overflowed or forcedly transferred from the uppermost purification treatment chamber 4 through the transfer means 71 under anaerobic conditions. Contains methane bacteria. The aerobic decomposition chamber 73 contains aerobic organisms that decompose residual organic components in the treated water led out from the anaerobic decomposition chamber 72 and nitrify ammonia. The treated water that has been decomposed by the aerobic biodegradation chamber 73 and led to the precipitation separation chamber 74 is subjected to precipitation treatment in the precipitation section adjacent chamber 74, and is then sprinkled or discharged, or recycled as fire prevention water or the like. Used.

また、上記嫌気分解室72には、その内部に収容された排水の一部を循環させる循環パイプ75が設けられている。この循環パイプ75には、ボイラ76から供給される廃熱または蒸気によって上記循環パイプ75内を循環する排水中の汚泥成分を70°C以上に加熱することにより、汚泥成分中の繊維質や角質の分解を促進するとともに、上記嫌気分解室72内の温度を、35°C〜37°C程度のメタン発酵菌による中温発酵に適した温度、または53°C〜56°C程度のメタン発酵菌による高温発酵に適した温度に加熱する加熱器77からなる加熱手段が設けられている。上記ボイラ76は、嫌気分解室72において生成されたメタンガスを燃料とし、上記浄化水貯留槽2内の浄化水を加熱することにより蒸気を生成するように構成されている。   The anaerobic decomposition chamber 72 is provided with a circulation pipe 75 that circulates a part of the drainage accommodated therein. The circulation pipe 75 is heated to 70 ° C. or higher with the sludge component in the waste water circulating in the circulation pipe 75 by waste heat or steam supplied from the boiler 76, so that the fibers and keratin in the sludge component are heated. The temperature in the anaerobic decomposition chamber 72 is a temperature suitable for medium temperature fermentation by methane fermentation bacteria of about 35 ° C. to 37 ° C., or methane fermentation bacteria of about 53 ° C. to 56 ° C. The heating means which consists of the heater 77 heated to the temperature suitable for high temperature fermentation by is provided. The boiler 76 is configured to generate steam by using the methane gas generated in the anaerobic decomposition chamber 72 as fuel and heating the purified water in the purified water storage tank 2.

上記の構成によれば、最上流浄化処理室4内から汚泥分解槽70に移送手段71を介して移送された排水中の汚泥成分を、上記嫌気分解室72、好気分解室73および沈殿分解室74内において段階的に浄化処理することにより、上記汚泥成分を効率よく分解処理することができるため、上記浄化処理槽1の処理能力を超えた排水が供給された場合においても、これを容易に浄化処理することができ、しかも上記嫌気分解室72において生成されたメタンガス等のバイオガスをボイラ76等の燃料として有効に利用することができるという利点がある。   According to said structure, the sludge component in the waste_water | drain transferred from the most upstream purification process chamber 4 to the sludge decomposition tank 70 via the transfer means 71 is made into the said anaerobic decomposition chamber 72, the aerobic decomposition chamber 73, and precipitation decomposition | disassembly. Since the sludge components can be efficiently decomposed by performing the purification process step by step in the chamber 74, even when waste water exceeding the treatment capacity of the purification tank 1 is supplied, Further, there is an advantage that biogas such as methane gas generated in the anaerobic decomposition chamber 72 can be effectively used as fuel for the boiler 76 and the like.

また、上記実施形態では、移送手段17を介して汚泥分解槽70の嫌気分解室72に移送された排水中の汚泥成分を70°C以上に加熱することにより、汚泥成分中の繊維質や核質の分解を促進する加熱手段77を設けたため、汚泥分解槽70の嫌気分解室72に移送された排水中の汚泥成分を所定温度に加熱して上記繊維質や核質の分解を促進することができるとともに、嫌気分解室75の内部をメタン菌の発酵作用に適した温度に加熱することにより、上記排水をさらに効果的に浄化処理できるという利点がある。   In the above embodiment, the sludge component in the wastewater transferred to the anaerobic decomposition chamber 72 of the sludge decomposition tank 70 via the transfer means 17 is heated to 70 ° C. or more, so that the fibers and nuclei in the sludge component are heated. Since the heating means 77 for promoting the decomposition of the quality is provided, the sludge components in the wastewater transferred to the anaerobic decomposition chamber 72 of the sludge decomposition tank 70 are heated to a predetermined temperature to promote the decomposition of the fibers and nuclei. In addition, there is an advantage that the waste water can be purified more effectively by heating the inside of the anaerobic decomposition chamber 75 to a temperature suitable for the fermentation action of methane bacteria.

排水浄化装置の全体構成を示す説明図である。It is explanatory drawing which shows the whole structure of a waste water purification apparatus. 上記排水浄化装置の全体構成を示す平面図である。It is a top view which shows the whole structure of the said waste water purification apparatus. 貝殻接触材を構成する貝殻の断面図である。It is sectional drawing of the shell which comprises a shell contact material. 貝殻の真珠層を除去した状態を示す断面図である。It is sectional drawing which shows the state which removed the pearl layer of the shell. 最下流浄化処理室に設けられた循環手段の具体的構成を示す斜視図である。It is a perspective view which shows the specific structure of the circulation means provided in the most downstream purification | cleaning processing chamber. 還流通路の具体的構成を示す正面図である。It is a front view which shows the specific structure of a recirculation | reflux channel | path. 排水浄化装置の別の例を示す平面図である。It is a top view which shows another example of a waste water purification apparatus. 活性炭収容体の設置例を示す説明図である。It is explanatory drawing which shows the example of installation of an activated carbon container. 活性炭収容体の別の設置例を示す説明図である。It is explanatory drawing which shows another example of installation of an activated carbon container. 排水浄化装置のさらに別の例を示す平面図である。It is a top view which shows another example of a waste water purification apparatus. 排水浄化装置のさらに別の例を示す平面図である。It is a top view which shows another example of a waste water purification apparatus. 排水浄化装置のさらに別の例を示す平面図である。It is a top view which shows another example of a waste water purification apparatus.

符号の説明Explanation of symbols

1 浄化処理槽
2 浄化水貯留槽
4 最上流浄化処理室
5 第1中流浄化処理室
6 第2中流浄化処理室
7 第3中流浄化処理室
8 最終浄化処理室
9 浄化水貯留室
DESCRIPTION OF SYMBOLS 1 Purification processing tank 2 Purified water storage tank 4 Uppermost stream purification processing chamber 5 1st middle flow purification treatment chamber 6 2nd middle flow purification treatment chamber 7 3rd middle flow purification treatment chamber 8 Final purification treatment chamber 9 Purified water storage chamber

Claims (1)

トイレから排出された汚水等の汚泥成分を含有する排水を段階的に浄化する複数の浄化処理室を備えた浄化処理槽と、この浄化処理槽とは別体に形成されるとともに、浄化処理槽から導出された浄化水を貯留する浄化水貯留槽とを有する排水浄化装置の洗浄方法であって、上記複数の浄化処理室の内部に収容された排水及び処理水の導出作業を行った後に、上記浄化水貯留槽内に貯留された浄化水を、浄化処理槽の最上流部に位置する最上流浄化処理室の上部から洗浄水として供給することにより、最上流浄化処理室の内壁面に付着した汚泥成分等を除去するとともに、最上流浄化処理室およびその下流側の浄化処理室内に上記浄化水からなる洗浄水を充填することを特徴とする排水浄化装置の洗浄方法。   A purification treatment tank having a plurality of purification treatment chambers for gradually purifying wastewater containing sludge components such as sewage discharged from the toilet, and the purification treatment tank are formed separately from the purification treatment tank. A purification method of a wastewater purification apparatus having a purified water storage tank for storing purified water derived from the water, and after conducting the drainage of the wastewater and treated water contained in the plurality of purification treatment chambers, The purified water stored in the purified water storage tank is attached to the inner wall of the uppermost purification chamber by supplying the cleaning water from the upper part of the uppermost purification chamber located in the uppermost stream of the purification tank. A cleaning method for a wastewater purification apparatus, wherein the sludge component and the like are removed, and the uppermost purification treatment chamber and the purification treatment chamber downstream thereof are filled with washing water comprising the purified water.
JP2006020647A 2006-01-30 2006-01-30 Washing method of wastewater treatment apparatus Pending JP2006218477A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008289969A (en) * 2007-05-23 2008-12-04 Eiwa Kokudo Kankyo Kk Container type sewage cleaning system
WO2023187881A1 (en) * 2022-03-28 2023-10-05 中国電力株式会社 Wastewater cleaning device and water recycling system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008289969A (en) * 2007-05-23 2008-12-04 Eiwa Kokudo Kankyo Kk Container type sewage cleaning system
WO2023187881A1 (en) * 2022-03-28 2023-10-05 中国電力株式会社 Wastewater cleaning device and water recycling system

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