JPH10272493A - Treatment of sewage and its treating device - Google Patents

Treatment of sewage and its treating device

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Publication number
JPH10272493A
JPH10272493A JP9114124A JP11412497A JPH10272493A JP H10272493 A JPH10272493 A JP H10272493A JP 9114124 A JP9114124 A JP 9114124A JP 11412497 A JP11412497 A JP 11412497A JP H10272493 A JPH10272493 A JP H10272493A
Authority
JP
Japan
Prior art keywords
water
inflow
sewage
outflow
drum
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.)
Pending
Application number
JP9114124A
Other languages
Japanese (ja)
Inventor
Takashi Takarabe
隆 財部
Hironori Nakatani
博宣 中谷
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.)
Tokai Rika Service Co Ltd
Original Assignee
Takara Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takara Industries Co Ltd filed Critical Takara Industries Co Ltd
Priority to JP9114124A priority Critical patent/JPH10272493A/en
Publication of JPH10272493A publication Critical patent/JPH10272493A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To generate suspended solids(SSs) and to easily and efficiently recover the SSs by adjusting the pH of the sewage, miscellaneous drainage, etc., from such as household, food industry and agricultural and industrial use. SOLUTION: This treatment method for the sewage consists in subjecting the sewage, etc., to pH adjustment with metal soap, such as slaked lime, to generate the insoluble SSs and treating the SSs by a physical treatment of a backwashing type. The treating device has a drum 3 of a horizontal type which is internally vertically formed with a filter tank 1 consisting of filter media to recover the SSs and a space section 2, a first inflow pipe 5 for the inflow of raw water commonly used for the outflow of the sewage of which the first inflow section 4 for the inflow of the raw water commonly used for the outflow of the sewage exists in the space section from its axial central part and a second inflow pipe 7 for the inflow of filtrate water commonly used of the outflow of washing water of which a second inflow section 6 for the inflow of filtrated water commonly used for the outflow of the washing water exists in the filter tank from its axial central part. Plate filter nets 8, such as wedge wires, which are rotationally supported by means of rails 50 and rollers 51 on the outer periphery of the drum and are communicated with the second inflow section 6 for the inflow of the filtrated water commonly used for the outflow of the washing water is installed to the device. Means for cleaning the rear surfaces of the filter nets 8 and preventing the adhesion of algae, etc., following up the rotation of the drum are installed between the filter nets 8 and the inside wall surfaces of the drum 3.

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、家庭汚水・雑排
水、食品工業用水、農漁、工業用水等の汚水をPH調整
して、浮遊物質を発生させ、該浮遊物質を逆洗式の物理
濾過により処理する方法とその処理装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for adjusting the pH of sewage such as domestic sewage / miscellaneous effluent, food industrial water, agricultural / fishing, industrial water, etc., to generate suspended solids, and to subject the suspended solids to backwashing physical treatment. The present invention relates to a method for processing by filtration and a processing apparatus therefor.

【0002】[0002]

【従来の技術】従来より、家庭排水、食品工業や農業・
漁業・工業用水等の排水・用水、雑排水等の汚水には油
や澱粉やタンパク質等を含有しているので、カセイソー
ダ等のPH調整して、アルカリ性を付与することによる
代表的ビルダーとしての水酸化ナトリウムにより、油と
水酸化ナトリウムは石鹸とグリセリンとなり、この石鹸
は弱アルカリ性であるため、化学的に油脂を可溶性に変
じ、また、油脂を小滴に分散乳状化し、粘着性の少ない
液とする。また、石鹸液は、粘いにわか質液であるた
め、物理的にじんあいを吸着して除去する、これらの働
きにより、物理濾過ができず、沈殿槽による沈殿処理し
ていた、しかし、排水量が多くなればなる程このような
沈殿槽は大規模となり、設置面積も広く管理や補修が大
変である。また、一種の物理的濾過装置である膜処理装
置のものでも生物処理槽が必要であり、膜処理装置や生
物処理槽によりコストアップとなる。そこで、この生物
処理槽を無くしても後処理としての活性炭処理装置が必
要か前処理の生物処理槽に代えて凝集処理装置が必要で
あった。これらの種々な処理装置の洗浄が不十分であっ
たり、濾材の洗浄に大容量の洗浄水と時間とを要した
り、浮遊物質の回収装置が複雑で種々の槽が必要とな
り、その処理装置が大型化すると云う欠点がある。な
お、上記の代表的なビルダーとしては、芒硝(Na
)、リン酸ナトリウム系各種(1例)(NaPO
・12HO)、水酸化ナトリウム(NaOH)、セ
スキ炭酸ナトリウム(NaCO・NaHCO・2H
O)、硅酸ナトリウム系各種(1例)(NaSi
)、カルボキシメチールセルロース(CMC)など
がある。
2. Description of the Related Art Conventionally, domestic wastewater, food industry, agriculture,
Wastewater such as fisheries / industrial water / wastewater / miscellaneous wastewater contains oil, starch, protein, etc., so water is used as a representative builder by adjusting the pH of caustic soda etc. to impart alkalinity. Due to sodium oxide, oil and sodium hydroxide become soap and glycerin.Since this soap is weakly alkaline, it chemically converts fats and oils to soluble, and also disperses the fats and oils into small droplets and emulsifies them with a less sticky liquid. I do. Also, since the soap solution is a viscous liquid, it physically removes dust by adsorbing it.Thus, due to these actions, physical filtration could not be performed, and the sedimentation treatment was performed using a sedimentation tank. The larger the number of such sedimentation tanks, the larger the installation area and the more difficult it is to manage and repair. In addition, a biological treatment tank is required even for a membrane treatment device that is a kind of physical filtration device, and the cost increases due to the membrane treatment device and the biological treatment tank. Therefore, even if this biological treatment tank is eliminated, an activated carbon treatment device is required as a post-treatment, or a coagulation treatment device is required in place of the pretreatment biological treatment tank. Cleaning of these various processing devices is inadequate, large amounts of washing water and time are required for cleaning the filter media, and a device for collecting suspended solids is complicated and various tanks are required. However, there is a disadvantage that the size is increased. In addition, as the above-mentioned representative builder, sodium sulfate (Na 2 S
O 4 ), various types of sodium phosphate (1 example) (Na 3 PO
4 · 12H 2 O), sodium hydroxide (NaOH), sodium sesquicarbonate (NaCO 3 · NaHCO 3 · 2H
2 O), various types of sodium silicate (1 example) (NaSi
O 2 ) and carboxymethyl cellulose (CMC).

【0003】また、水産廃水をPH調整した後に蛋白凝
集剤を添加して高速攪拌して凝集蛋白を分離させる処理
方法(特公昭55−6435号公報)があるが、高速攪
拌とその回収が大変である。さらに、PH調整され、又
は凝集剤が添加されている有機排水からBOD、CO
D、N−H(ノルマルヘキサン可溶性物質即ち油脂性物
質)及び浮遊固形物質を除去するに、この処理排水をジ
ェットエジェクターの中へ加圧下に噴出させ、該噴出に
よって減圧状態を形成させ、該状態下に空気吸入及び高
分子凝集剤溶液の吸入を伴いながら水面に落下させ、浮
遊固形物質を浮上分離させるもの(特公平7−1213
87号公報)があるが、このものもその回収が大変であ
る。さらには、特公平7−41255号公報のように
か、種々の処理槽を垂直方向に設けることで、従来の3
0%程度の面積にせんとするものであるが、やはり上述
のように濾材の洗浄が不十分であったり、濾材の洗浄に
大容量の洗浄水と時間とを要したり、それらの装置が複
雑で大型化すると云う欠点がある。特開平6−2697
99号公報や特公平7−102358号公報等もある
が、溶解性リンを固定化せんとしたり、凝集水を膜濾過
して処理水を凝集槽や貯留槽に戻していたものである。
それらの装置が複雑で大型化すると云う欠点がある。
[0003] Further, there is a treatment method in which a protein flocculant is added after the pH of marine wastewater is adjusted, followed by high-speed stirring to separate the flocculated proteins (Japanese Patent Publication No. 55-6435). However, high-speed stirring and recovery thereof are very difficult. It is. In addition, BOD, CO is removed from the organic wastewater to which the pH is adjusted or a coagulant is added.
In order to remove D, NH (normal hexane soluble substance or oily substance) and suspended solid substances, this treated wastewater is ejected under pressure into a jet ejector, and the ejected liquid forms a reduced pressure state. A device which is dropped on the water surface while inhaling air and inhaling a polymer flocculant solution under the air to separate suspended solid matter by floating (Japanese Patent Publication No. 7-1213).
No. 87), but it is also difficult to recover them. Further, as disclosed in Japanese Patent Publication No. 7-41255, various treatment tanks are provided in a vertical direction, so that the conventional 3
Although it is intended to cover an area of about 0%, as described above, the washing of the filter medium is insufficient, the washing of the filter medium requires a large amount of washing water and time, and such a device is used. There is a disadvantage that it is complicated and large. JP-A-6-2697
No. 99 and Japanese Patent Publication No. 7-102358, etc., in which soluble phosphorus is immobilized, or coagulated water is subjected to membrane filtration to return treated water to a coagulation tank or a storage tank.
The disadvantage is that these devices are complicated and large.

【0004】本願発明者等は、さきに、濾過網の面積を
拡げて濾過効率を上げるとともに、逆洗時に濾過網に濾
材を摺動接触させて、無理なく濾過網に付着した汚物や
懸濁物等を破壊し除去でき、かつ従来の固定式で逆洗式
濾過装置に比べて略1/10という少ない洗浄水で濾材
の洗浄が可能な回転式で逆洗式濾過装置を提案した。ま
た、濾過網をウェジワイヤーであって、洗浄時にドラム
の内部で粒状濾材同志の擦り合わせを発生させ、粒状濾
材を破壊することなく、それでいて捕集された懸濁物を
より無理なく簡単に略完全に除去できる濾過装置をも提
案した。また、ドラムの内壁と濾過網の裏面とは間隔が
なく、濾過網の裏側まで洗浄するものではないので、長
期の使用時にどうしても濾過網の裏面に汚物が着いた
り、藻類等が付着したり、黴等の発生の原因ともなって
いた。そこで、板状の濾過網とドラムの内壁間に濾過時
も濾過網の裏面の自浄機能と藻類等の付着防止機能とを
有することで、汚れや藻類等が付着したり、黴等が発生
することを防止すると共に汚れ等が付着してもドラムの
回転により自動的に洗浄してくれる濾過装置を提案し
た。そこで、家庭等の汚水には油や澱粉やタンパク質等
を含有しているので、消石灰等の金属石鹸でPH調整し
て、不溶解性浮遊物質を発生させ、該浮遊物質を上述の
回転式の種々な逆洗式濾過手段により効率的に処理でき
ることを知見した。
[0004] The inventors of the present application have previously increased the filtration efficiency by enlarging the area of the filter net and, at the same time, sliding the filter medium into contact with the filter medium during backwashing, thereby making it easier for the dirt and suspended matter adhering to the filter net to come into contact. We have proposed a rotary backwash type filtration device that can destroy and remove objects and the like, and can wash the filter medium with less washing water, which is about 1/10 that of a conventional fixed type backwash type filtration device. In addition, the filter net is a wedge wire, which causes the rubbing of the granular filter media inside the drum during washing, without destroying the granular filter media, and making the collected suspension more easily and easily. A filtration device that can be removed almost completely has also been proposed. In addition, since there is no gap between the inner wall of the drum and the back of the filtration net, and it is not intended to wash the back of the filtration net, filth may inevitably arrive on the back of the filtration net during long-term use, or algae or the like may adhere. This was a cause of mold and the like. Therefore, even when filtration is performed between the plate-shaped filtration net and the inner wall of the drum, the filter has a self-cleaning function of the back surface of the filtration net and a function of preventing adhesion of algae, etc. We have proposed a filtration device that prevents this and automatically cleans by rotating the drum even if dirt etc. adhere. Therefore, since household wastewater contains oil, starch, protein, etc., the pH is adjusted with a metal soap such as slaked lime to generate insoluble floating substances, and the floating substances are converted to the above-mentioned rotary type. It has been found that the treatment can be efficiently performed by various backwashing filtration means.

【0005】[0005]

【発明が解決しようとする課題】第1に、従来のような
大規模な沈殿槽を必要とせず、物理的濾過手段の採用で
大規模な沈殿槽を小形化するか不要とし、又は生物処理
槽をも必ずしも必要とせず使用しても同じ処理規模でも
従来の1/3程度の大幅削減し、さらに物理的濾過では
できないとされていた汚水をPH調整して、不溶解性の
浮遊物質を発生させ、該浮遊物質を簡単に物理的処理す
る汚水の処理方法を提供すること。第2に、従来のよう
な大規模な沈殿槽を必要とせず、物理的濾過手段の採用
で大規模な沈殿槽を小形化するか不要とし、又は生物処
理槽をも必ずしも必要とせず、物理的濾過ではできない
とされていた汚水を消石灰等の金属石鹸でPH調整し
て、不溶解性の浮遊物質を発生させ、該浮遊物質を簡単
に回転式の逆洗式濾過により物理的処理する汚水の処理
方法を提供すること。第3に、第1又は第2の課題に加
えて、予備的沈殿槽と必要に応じて大幅削減した生物処
理槽で処理した後に殺菌するだけで用水或いは中水用水
に利用できる汚水の処理方法を提供すること。第4に、
浮遊物質等を濾過するに、濾過網の面積を拡げて濾過効
率を上げるとともに、逆洗時に濾材同志を擦り合せて濾
材から付着物を分離させ濾材の復元を完全に行い、無理
なく濾過網に付着した汚物や懸濁物等を破壊し除去で
き、かつ従来の固定式で逆洗式濾過装置に比べて略1/
10の少ない洗浄水で濾材の洗浄が可能で、確実に効率
的に浮遊物質を回収する汚水の処理装置を提供するこ
と。第5に、第4の課題に加えて、濾槽内と空間部内と
に板状の濾過網を設けたので、濾過が荒い濾過と濾槽内
の濾過との二重濾過ができると共に、逆洗時にこれら板
状の濾過網に付着物質を自動的に洗浄する汚水の処理装
置を提供すること。第6に、第4又は第5の課題に加え
て、原水流入兼汚水流出用第1流水管と、濾水流入兼洗
浄水流出用第2流水管とのいずれか一方又は両方を横型
のドラムの外に配設したので、ドラム内にデットスペー
スを少なく又は全くつくらないので、より小形化が可能
とした汚水の処理装置を提供すること。第7に、第4乃
至第6のいずれかの課題に加えて、ドラムの内壁間に濾
過時も濾過網の裏面の自浄機能と藻類等の付着防止機能
とを有することで、汚れや藻類等が付着したり、黴等が
発生することを防止すると共に汚れ等が付着してもドラ
ムの回転により自動的に洗浄してくれる処理装置なの
で、より確実に清潔な汚水の処理装置を提供すること。
第8に、第7の課題に加えて、付着物付着防止手段を防
ばい剤を混入或いは被覆したことで、常に清潔に保てる
汚水の処理装置を提供すること。第9に、第4乃至第8
のいずれかの課題に加えて、濾過網に防ばい剤を混入或
いは被覆するだけで、濾過網の裏面の清掃が長時間不要
で藻類等の付着物防止がより確実にできる汚水の処理装
置を提供すること。第10に、第4乃至第9のいずれか
の課題に加えて、原水流入兼汚水流出用第1流水管又は
濾水流入兼洗浄水流出用第2流水管に、原水及び洗浄水
流入又は処理水及び洗浄水流出時に全開となり汚水流出
又は洗浄水流入時に絞り開口となる弁を付設したので、
流量の調節を自動化し、洗浄水の節約を計った汚水の処
理装置を提供すること。第11に、第10の課題に加え
て、弁の構造を簡単にすると共に、浮遊物質の付着をも
減らすことができる汚水の処理装置を提供すること。第
12に、第4乃至第11のいずれかの課題に加えて、原
水流入兼汚水流出用第1流水管の取り付け角度を、粒状
濾材の上方で濾材安定角よりドラムの回転方向へ略90
度の範囲内としたので、逆洗時の粒状濾材の崩落による
濾材の巻上げがあっても、粒状濾材の流出を防止するこ
とができる汚水の処理装置を提供すること。第13に、
第4乃至第12のいずれかの課題に加えて、前記ドラム
の外周に少なくとも1条のレールを付設し、該レールを
案内するガイドを設けたローラで支持したので、回転軸
のセンターだしが楽にてぎ、駆動部側のカムフロアー等
を不要とし機構を簡潔にでき、故障のすくない汚水の処
理装置を提供すること。第14に、第4乃至第13のい
ずれかの課題に加えて、濾材がドラムの回転を支持する
流水管の軸受部に入込むのを防止し、簡単な構造で、長
期の使用に耐え、メンテナンスの楽な耐久性がよい汚水
の処理装置を提供すること。
First, there is no need for a large-scale sedimentation tank as in the prior art, and the size of the large-scale sedimentation tank can be reduced or eliminated by employing physical filtration means. Even if the tank is not necessarily required and used, the same treatment scale can be greatly reduced by about one-third compared to the conventional one, and the pH of wastewater, which was considered impossible by physical filtration, can be adjusted to reduce insoluble suspended solids. Provided is a method for treating wastewater that generates and easily physically treats the suspended matter. Second, it does not require a large-scale sedimentation tank as in the prior art, and uses a physical filtration means to reduce or eliminate the need for a large-scale sedimentation tank, and does not necessarily require a biological treatment tank. Sewage that is considered to be impossible by mechanical filtration, pH is adjusted with metal soap such as slaked lime to generate insoluble suspended solids, and the suspended solids are physically treated by a simple rotary backwash filtration. To provide a processing method. Third, in addition to the first or second problem, a method for treating wastewater that can be used for service water or municipal water simply by sterilizing after treating in a preliminary sedimentation tank and a biological treatment tank that is greatly reduced as necessary. To provide. Fourth,
To filter suspended substances, etc., increase the filtration area by increasing the area of the filtration network, and at the same time, rub the filter media together during backwash to separate the deposits from the filter media and completely restore the filter media. Adhered dirt and suspended matter can be destroyed and removed, and it is almost 1 /
Provided is a sewage treatment apparatus capable of washing a filter medium with as little as 10 washing waters and recovering suspended solids reliably and efficiently. Fifth, in addition to the fourth problem, a plate-like filtration network is provided in the filter tank and the space, so that double filtration of coarse filtration and filtration in the filter tank can be performed. Provided is a sewage treatment apparatus for automatically washing adhered substances to these plate-shaped filtration nets during washing. Sixth, in addition to the fourth or fifth problem, one or both of a first flowing pipe for raw water inflow and sewage outflow and a second flowing water pipe for infiltration inflow and washing water outflow are provided with a horizontal drum. The present invention provides a wastewater treatment apparatus that can be made more compact because it has no or no dead space in the drum because it is disposed outside the drum. Seventh, in addition to any of the fourth to sixth problems, the filter has a self-cleaning function of the back surface of the filtration network and a function of preventing adhesion of algae and the like even when filtering between the inner walls of the drum, so that dirt, algae and the like can be prevented. Provide a more reliable and clean sewage treatment device because it is a processing device that prevents the adhesion of molds and molds, and automatically cleans by rotating the drum even if dirt is attached. .
Eighth, in addition to the seventh object, to provide a sewage treatment apparatus that can always keep clean by mixing or covering an antifouling agent in the adhesion preventing means. Ninth, fourth to eighth
In addition to any of the above-mentioned problems, a sewage treatment apparatus capable of cleaning the back of the filtration network for a long time without the need of cleaning for a long period of time and ensuring the prevention of deposits such as algae by simply mixing or covering the filtration network with a deterrent agent. To provide. Tenthly, in addition to any of the fourth to ninth problems, raw water and washing water are introduced or treated into a first flowing pipe for raw water inflow and sewage outflow or a second flowing water pipe for filtered water inflow and washing water outflow. A valve that opens fully when water and washing water flows out and becomes a throttle opening when sewage or washing water flows in is attached.
To provide a sewage treatment apparatus that automatically adjusts a flow rate and saves washing water. Eleventh, in addition to the tenth problem, to provide a sewage treatment apparatus capable of simplifying the structure of a valve and reducing adhesion of suspended matter. Twelfth, in addition to any of the fourth to eleventh problems, the mounting angle of the first flowing water pipe for raw water inflow and sewage outflow is set to approximately 90 degrees above the granular filter medium from the filter medium stable angle in the direction of rotation of the drum.
Provided is a sewage treatment apparatus capable of preventing the granular filter medium from flowing out even if the filter medium is rolled up due to collapse of the granular filter medium during backwashing. Thirteenth,
In addition to the fourth to twelfth problems, at least one rail is provided on the outer periphery of the drum, and the drum is supported by a roller provided with a guide for guiding the rail. An object of the present invention is to provide a sewage treatment apparatus that does not require a cam floor or the like on a drive unit side, can simplify a mechanism, and is free from trouble. Fourteenth, in addition to any of the fourth to thirteenth problems, the filter medium is prevented from entering a bearing portion of a water pipe supporting rotation of the drum, has a simple structure, and can withstand long-term use. Provide a durable sewage treatment device that is easy to maintain.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
するために、第1に、汚水をPH調整して、不溶解性浮
遊物質を発生させ、該浮遊物質を逆洗式物理濾過により
処理したことを特徴とする汚水の処理方法である。第2
に、汚水を消石灰等の金属石鹸でPH調整して、不溶解
性浮遊物質を発生させ、該浮遊物質を回転式の逆洗式濾
過手段により処理したことを特徴とする汚水の処理方法
である。第3に、汚水を沈殿槽に予備的に貯槽し、消石
灰等の金属石鹸でPH調整して、不溶解性浮遊物質を発
生させ、該浮遊物質を直接回転式の逆洗式濾過手段によ
り処理し、該処理水を必要に応じて生物処理槽で処理し
た後に殺菌して用水或いは中水用水としたことを特徴と
する汚水の処理方法である。第4に、前記回転式の逆洗
式濾過手段として、粒状濾材からなる濾槽と空間部とが
内部上下方向に形成されている横型のドラムと、この横
型のドラムの外からその軸心部より原水流入兼汚水流出
用第1流水部が空間部内に位置している原水流入兼汚水
流出用第1流水管と、前記横型のドラムの外からその軸
心部より濾水流入兼洗浄水流出用第2流水部が濾槽内に
位置している濾水流入兼洗浄水流出用第2流水管とを有
する濾過装置において、前記濾槽内には前記横型のドラ
ムと共に回転し、前記濾水流入兼洗浄水流出用第2流水
部と連通する板状の濾過網を付設したことを特徴とする
汚水の処理装置である。第5に、前記濾槽内と空間部内
とには前記横型のドラムと共に回転し、濾槽内では前記
濾水流入兼洗浄水流出用第2流水部と連通する板状の濾
過網を付設し、空間部内では原水流入兼汚水流出用第1
流水管と連通する板状の濾過網を付設したことを特徴と
する請求項4に記載の汚水の処理装置である。第6に、
前記原水流入兼汚水流出用第1流水管と、濾水流入兼洗
浄水流出用第2流水管とのいずれか一方又は両方が横型
のドラムの外に配設し、該配設が濾槽内に位置している
原水流入兼汚水流出用第1流水部又は濾水流入兼洗浄水
流出用第2流水部と連通させたことを特徴とする請求項
4又は請求項5に記載の汚水の処理装置である。第7
に、前記濾槽内には前記横型のドラムと共に回転し、前
記濾水流入兼洗浄水流出用第2流水部と連通するウェッ
ジワイヤー等の板状の濾過網を付設し、該板状の濾過網
とドラムの内壁間にドラムの回転に追従する濾過網の裏
面の清掃藻類等のブラシ等の付着物防止手段を設けたこ
とを特徴とする請求項4乃至請求項6のいずれか1項に
記載の汚水の処理装置そである。第8に、前記清掃・藻
類等の付着物防止手段に防ばい剤等を混入或いは被覆し
たことを特徴とする請求項7に記載の汚水の処理装置で
ある。第9に、前記板状の濾過網に防ばい剤等を混入或
いは被覆したことを特徴とする請求項4乃至請求項8の
いずれか1項に記載の汚水の処理装置である。第10
に、前記原水流入兼汚水流出用第1流水管又は濾水流入
兼洗浄水流出用第2流水管に、原水流入又は洗浄水流出
時に全開となり汚水流出又は濾水流入時に絞り開口とな
る弁を付設したことを特徴とする請求項4乃至請求項9
のいずれか1項に記載の汚水の処理装置である。第11
に、前記弁は、バタフライ弁に所望の径の孔を穿設し、
原水流入又は洗浄水流出時の全開時はバタフライ弁とし
て機能し、汚水流出又は濾水流入時の絞り開口時には所
望の径の孔による少流量として機能させたことを特徴と
する請求項10に記載の汚水の処理装置である。第12
に、前記原水流入兼汚水流出用第1流水管の取り付け角
度を、粒状濾材の上方で濾材の安定角よりドラムの回転
方向へ略90度の範囲内としたことを特徴とする請求項
4乃至請求項11のいずれか1項に記載の汚水の処理装
置である。第13に、前記ドラムの外周に少なくとも1
条のレールを付設し、該レールを案内するガイドを設け
たローラで支持したことを特徴とする請求項4乃至請求
項12のいずれか1項に記載の汚水の処理装置である。
第14に、前記横型のドラムの回転を支持する軸心部と
して機能する原水流入兼汚水流出用第1流水管の内測に
防砂パッキンを装着したことを特徴とする請求項4乃至
請求項13のいずれか1項に記載の汚水の処理装置であ
る。
In order to solve the above-mentioned problems, the present invention firstly adjusts the pH of sewage to generate insoluble suspended substances, and the suspended substances are subjected to backwashing physical filtration. A wastewater treatment method characterized by being treated. Second
The pH of the wastewater is adjusted with a metal soap such as slaked lime to generate an insoluble suspended substance, and the suspended substance is treated by a rotary backwashing filtration means. . Third, sewage is preliminarily stored in a sedimentation tank, and the pH is adjusted with a metal soap such as slaked lime to generate insoluble suspended substances, and the suspended substances are directly treated by a rotary backwashing filtration means. Then, the treated water is treated in a biological treatment tank as required, and then sterilized to make it into service water or tap water. Fourth, as the rotary backwashing filtration means, a horizontal drum in which a filter tank made of a granular filter medium and a space are formed in the vertical direction inside, and an axial center portion of the horizontal drum from outside. A first flow pipe for raw water inflow and sewage discharge in which the first flow section for raw water inflow and sewage discharge is located in the space; A second flowing water pipe for draining and inflowing the washing water, wherein the second flowing water section is located in the filtering tank, wherein the filtering tank rotates together with the horizontal drum in the filtering tank, A sewage treatment apparatus characterized in that a plate-shaped filtration network communicating with a second flowing water section for inflow and washing water outflow is provided. Fifthly, a plate-shaped filter net that rotates together with the horizontal drum in the filter tank and the space and communicates with the second flowing water section for inflow of filtrate and outflow of wash water is provided in the filter tank. The first for raw water inflow and sewage outflow in the space
The sewage treatment apparatus according to claim 4, further comprising a plate-shaped filtration network that communicates with the flowing water pipe. Sixth,
Either or both of the first flow pipe for raw water inflow and sewage discharge and the second flow pipe for filtrate inflow and washing water outflow are disposed outside the horizontal drum, and the distribution is in the filtration tank. 6. The sewage treatment according to claim 4, wherein the effluent is communicated with a first flowing section for raw water inflow and sewage outflow or a second flowing section for filtered water inflow and washing water outflow. Device. Seventh
In addition, a plate-shaped filtration network such as a wedge wire, which is rotated together with the horizontal drum and communicates with the second flowing water portion for the filtration water inflow and the washing water outflow, is provided in the filtration tank. 7. A method according to claim 4, further comprising a means for removing a deposit such as a brush for cleaning algae or the like on the back surface of the filtration net following the rotation of the drum between the net and the inner wall of the drum. The wastewater treatment device described in the above. Eighthly, the sewage treatment apparatus according to claim 7, wherein a deodorizing agent or the like is mixed or covered with the means for preventing attachments such as cleaning and algae. Ninth, the sewage treatment apparatus according to any one of claims 4 to 8, wherein a screening agent or the like is mixed or covered with the plate-shaped filtration net. Tenth
The first water pipe for raw water inflow and sewage outflow or the second water pipe for filtrate inflow and rinsing water outflow is provided with a valve which is fully opened at the time of raw water inflow or cleaning water outflow and becomes a throttle opening at the time of sewage outflow or filtration water inflow. 10. An apparatus according to claim 4, wherein said apparatus is provided.
The sewage treatment apparatus according to any one of the above. Eleventh
In the valve, a hole having a desired diameter is formed in the butterfly valve,
11. The function as a butterfly valve when fully opened at the time of raw water inflow or washing water outflow, and at the time of throttle opening at the time of sewage outflow or filtered water inflow, a small flow rate through a hole of a desired diameter. Wastewater treatment equipment. Twelfth
The angle of attachment of the first flowing water pipe for raw water inflow and sewage discharge is within a range of approximately 90 degrees in the rotation direction of the drum from the stable angle of the filter medium above the granular filter medium. A sewage treatment apparatus according to claim 11. Thirteenth, at least 1
The sewage treatment apparatus according to any one of claims 4 to 12, wherein a strip rail is provided and supported by a roller provided with a guide for guiding the rail.
Fourteenthly, a sandproof packing is attached to the inside of the first water pipe for raw water inflow and sewage discharge, which functions as an axis supporting the rotation of the horizontal drum. The sewage treatment apparatus according to any one of the above.

【0007】[0007]

【実施の形態】以下、本発明の汚水の処理方法とその処
理装置について、図1乃至図17の各実施例に基ずいて
説明する。汚水とは、一般に大小便の排水を言い、家庭
等からの排水は雑排水と言われているが、本願発明にお
いては、これらの汚水、雑排水の他に、食品工業、農・
工業用水等からの排水をも含めて、以下単に、「汚水」
という。このような汚水は、一般に、表1に示すような
種々な処理をされて放流されるか中水等に再利用されて
いる。しかし、これらのものでは大規模な沈殿槽が必要
だったり、一種の物理的濾過装置である膜処理装置のも
のでも生物処理槽が必要であり、この生物処理槽を無く
しても後処理としての活性炭処理装置が必要か前処理の
生物処理槽に代えて凝集処理装置が必要であった。特に
沈殿槽は大型のものを必要とし、かつ、生物処理槽も大
型化し、その設置面積を広くせねばならなく、コストア
ップになっていた。また、これらの生物処理槽、沈殿
槽、凝集処理装置等の管理・補修等には時間と労力と費
用とがかかるものである、そこで、家庭等の汚水をPH
調整して、不溶解性浮遊物質を発生させ、該浮遊物質を
逆洗式の物理濾過により処理したことである。このPH
調整や物理濾過として好ましくは、消石灰等の金属石鹸
と回転式の逆洗式濾過装置とするとよい。さらに、汚水
を沈殿槽に予備的に貯槽し、消石灰等の金属石鹸でPH
調整して、不溶解性浮遊物質を発生させ、該浮遊物質を
直接回転式の逆洗式濾過手段により処理し、該処理水を
必要に応じて生物処理槽で処理した後に殺菌して用水或
いは中水用水とした汚水の処理方法である。なお、図示
していないが、逆洗式濾過手段の逆流水により剥離され
た付着物は排水管を経て槽外へ排出される際にスクリー
ン等で除去し、付着物を除去された洗浄汚水のみを予備
的沈殿槽に戻すとよい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A wastewater treatment method and a wastewater treatment apparatus according to the present invention will be described below with reference to the embodiments shown in FIGS. Sewage generally refers to wastewater of large and small stools, and wastewater from homes and the like is called miscellaneous wastewater. In the present invention, in addition to these wastewater and miscellaneous wastewater, food industry, agriculture,
In the following, including wastewater from industrial water, etc.,
That. Such sewage is generally subjected to various treatments as shown in Table 1 before being discharged or reused as middle water or the like. However, these require a large-scale sedimentation tank, and a biological treatment tank is required even for a membrane treatment device that is a kind of physical filtration device. Whether an activated carbon treatment device was required or not. A coagulation treatment device was required instead of the pretreatment biological treatment tank. In particular, a large sedimentation tank was required, and the biological treatment tank was also increased in size, so that the installation area had to be widened and the cost was increased. In addition, it takes time, labor, and cost to manage and repair these biological treatment tanks, sedimentation tanks, coagulation treatment devices, etc.
This was adjusted to generate insoluble suspended solids, and the suspended solids were treated by backwashing physical filtration. This PH
It is preferable to use a metal soap such as slaked lime and a rotary backwash type filtration device for adjustment and physical filtration. Further, the wastewater is preliminarily stored in a sedimentation tank, and the pH is adjusted with a metal soap such as slaked lime.
Adjust to generate insoluble suspended solids, treat the suspended solids directly with a rotary backwash filtration means, treat the treated water in a biological treatment tank if necessary, and then sterilize it with water or This is a method for treating sewage used as tap water. Although not shown, the deposits separated by the backflow water of the backwashing filtration means are removed by a screen or the like when discharged to the outside of the tank through the drain pipe, and only the washed wastewater from which the deposits have been removed is removed. May be returned to the preliminary settling tank.

【0008】[0008]

【表1】 [Table 1]

【0009】さらに、好適な処理装置として図1乃至図
3に示すように、粒状濾材からなる濾槽1と空間部2と
が内部上下方向に形成されている横型のドラム3と、こ
の横型のドラム3の外からその軸心部を貫通し原水流入
兼汚水流出用第1流水部4が空間部2内に位置している
原水流入兼汚水流出用第1流水管5と、前記横型のドラ
ム3の外からその軸心部を貫通し濾水流入兼洗浄水流出
用第2流水部6が濾槽1内に位置している濾水流入兼洗
浄水流出用第2流水管7とを有する濾過装置において、
板状の種々(例えば金網、金属製や合成樹脂製の多孔板
等)な濾過網8を横型のドラム3の濾槽1内に直接或い
はフランジ等にボルト・ナットや溶接或いは接着等で取
付けられ、或いは好ましくは蓋9の内面の略全面に蓋の
4方端に設けた口字状の部材やフランジ10を介して溶
接等で固定され、または、濾槽1内に或いは蓋9の内面
にボルト・ナット11等で着脱自在に付設してある。こ
の口字状の部材やフランジ10によって濾過網8は、横
型のドラム3の内面と略面一に付設されている。また、
濾過網8と蓋9との間隙13に濾過された濾水が集水さ
れ又は洗浄水(原水でもよい、以下洗浄水という)を通
水させるため濾水流入兼洗浄水流出用第2流水部6と連
通されている。この蓋9は横型のドラム3にボルト・ナ
ット12等で着脱自在に取付けられている。さらに、図
9乃至図12に示すように、原水流入兼汚水流出用第1
流水部4に板状の種々(例えば金網、金属製や合成樹脂
製の多孔板等で、好ましくはウェッジワイヤー)な濾過
網8、即ちウェッジワイヤー8は板に切込み8a…、8
b…により形成された多数のスリット8c…とで構成さ
れ、この板の上下左右の縁部を部材やフランジ10を介
してボルト・ナットで交換自在に取り付け、図12の
(ロ)の一部にスリット8cが設けられているが、この
スリット8cを穿設していない部位8dを設け、この部
位8dに短管8eを溶接等で取り付けて、さらにこの短
管8eの他端を第2流水管7に嵌合させることで蓋が着
脱自在に取り付けられている。またウェッジワイヤー8
の裏面には、図10に示すように、スリット方向に対し
て直角方向に補強桟8fを所望間隔おきに設けてあり、
さらに濾材や処理水の加重により耐えれるようにスリッ
ト方向にも補強桟8gを設けてもよい。そして横型のド
ラム3の濾槽1内に直接或いはフランジ10等で溶接或
いは接着、ボルト・ナット11等で固定され、或いは好
ましくは蓋9の内面の略全面に蓋の4方端に設けた口字
状の部材やフランジ10を介して溶接等で固定され、ま
たは、濾槽1内に或いは蓋9の内面にボルト・ナット1
1等で着脱自在に付設し、原水流入兼汚水流出部位でも
補助的な濾過手段を付設してもよい。この横型のドラム
3と原水流入兼汚水流出用第1流水管5とは図6に示す
ようなダストシール14、グランドパッキング15等を
介在させた軸受け16で嵌合させ、軸受け16と横型の
ドラム3の端壁とが固定されているとともに、該軸受け
16を付設されているギヤスプロケット17をモータ1
8の駆動力で回転(プーリとベルト駆動でもよい)させ
ることで、基台19の支持枠20上で、支持枠20に1
20度間隔に取付けた3個(大型の場合は6個等でもよ
い)のカムフォロア(球面外輪)21…により横型のド
ラム3を回転自在に支持させてある。また、濾過網8と
連通されている濾水流入兼洗浄水流出用第2流水部6が
濾槽1内に位置し、該濾水流入兼洗浄水流出用第2流水
部6と連通させる濾水流入兼洗浄水流出用第2流水管7
を横型のドラム3の他端に軸受け22と一体的に固定さ
れ、該軸受け22と基台19の支持枠20上で、横型の
ドラム3を回転自在に支持させてある。なお、このもの
においても後述の濾過網の裏面の清掃・藻類等の付着物
防止手段を施してもよい。
Further, as shown in FIGS. 1 to 3, as a preferred processing apparatus, a horizontal drum 3 in which a filter tank 1 made of a granular filter medium and a space portion 2 are formed in an up-down direction, A first flow pipe 5 for raw water inflow and sewage discharge, in which a first flow section 4 for raw water inflow and sewage discharge is penetrated from the outside of the drum 3 through the axial center thereof and is located in the space 2, and the horizontal drum 3 has a second flowing water pipe 6 for draining inflow and washing water, which is penetrated from the outside through the axial center thereof and is located in the filter tank 1. In the filtration device,
Various plate-like (for example, wire mesh, perforated plate made of metal or synthetic resin, etc.) filter nets 8 are attached directly to the filter tank 1 of the horizontal drum 3 or to a flange or the like by bolts and nuts, welding or bonding. Or, preferably, it is fixed to substantially the entire inner surface of the lid 9 by welding or the like via a bracket-shaped member or a flange 10 provided at the four ends of the lid, or in the filter tank 1 or on the inner surface of the lid 9. It is detachably attached with bolts and nuts 11 and the like. The filter net 8 is provided substantially flush with the inner surface of the horizontal drum 3 by the bracket-shaped member and the flange 10. Also,
The second drainage part for inflow of drainage and outflow of washing water for collecting or filtering the filtered water in the gap 13 between the filtration network 8 and the lid 9 or passing washing water (may be raw water, hereinafter referred to as washing water). It is communicated with 6. The lid 9 is detachably attached to the horizontal drum 3 with bolts and nuts 12 or the like. Further, as shown in FIG. 9 to FIG.
In the flowing water portion 4, various plate-shaped (for example, a wire mesh, a perforated plate made of metal or synthetic resin or the like, preferably a wedge wire), that is, a filtration network 8, that is, the wedge wire 8 is cut into the plate 8a.
.., and the upper, lower, left, and right edges of this plate are exchangeably attached with bolts and nuts via members and flanges 10, and a part of FIG. Is provided with a portion 8d where the slit 8c is not formed, a short pipe 8e is attached to this portion 8d by welding or the like, and the other end of the short pipe 8e is connected to the second flowing water. The lid is detachably attached by fitting to the tube 7. Also wedge wire 8
As shown in FIG. 10, reinforcing bars 8 f are provided at desired intervals in a direction perpendicular to the slit direction on the back surface of
Further, a reinforcing bar 8g may be provided in the slit direction so as to withstand the load of the filter medium and the treated water. Then, it is welded or adhered to the filter tank 1 of the horizontal drum 3 directly or by a flange 10 or the like, or is fixed by a bolt / nut 11 or the like, or preferably, a port provided at the four ends of the lid on substantially the entire inner surface of the lid 9. It is fixed by welding or the like via a U-shaped member or a flange 10, or a bolt and nut 1 is mounted in the filter tank 1 or on the inner surface of the lid 9.
1 and the like, which may be detachably attached, and an auxiliary filtration means may be additionally attached to the raw water inflow / sewage outflow site. The horizontal drum 3 and the first flush pipe 5 for raw water inflow and sewage discharge are fitted by a bearing 16 having a dust seal 14 and a gland packing 15 as shown in FIG. The gear sprocket 17 provided with the bearing 16 and the end wall of the motor 1
By rotating with a driving force of 8 (or a pulley and a belt may be driven), the support frame 20 of the base 19 is
The horizontal drum 3 is rotatably supported by three cam followers (spherical outer ring) 21... Attached at intervals of 20 degrees (or six in the case of a large size). Further, a second flowing water section 6 for draining inflow and washing water, which is in communication with the filtration network 8, is located in the filter tank 1, and a filter for communicating with the second flowing section 6 for draining inflow and washing water outflow. Second flowing water pipe 7 for water inflow and cleaning water outflow
Is fixed to the other end of the horizontal drum 3 integrally with the bearing 22, and the horizontal drum 3 is rotatably supported on the bearing 22 and the support frame 20 of the base 19. In this case, a means for cleaning the back surface of the filtration net and preventing foreign substances such as algae, which will be described later, may be applied.

【0010】また、図1、図4に示すように、横型のド
ラム3の外周に少なくとも1条で好ましくは2本のレー
ル50を付設し、該レール50を案内する好ましくは対
のガイド溝51a、52aを設けたローラ51、52で
支持した、この対のガイド溝ローラ51、52はU字型
の枠53、54に軸55、56で回動自在に取り付けら
れ、これらの枠は上記レール50を挟持するように基台
19上に溶接等で取り付けてある。また、図示していな
いがレールを凹溝とし、ローラを凸としてもよいので、
以下、レールとガイドを設けたローラとは上述の両者を
含む。このような横型の遊びのあるドラム3の支持によ
り、ドラムの回転軸のセンターだしが楽にでき、濾過槽
や配管等の総重量を下部で支えているので濾過槽の大型
化が可能となり、大規模な汚水処理を可能とし、駆動部
側のカムフロアー等の負担を軽減し、機構を簡潔にで
き、故障の少ない処理装置ができる。なお、前後左右に
遊びのあるドラム3の支持にしたので、原水流入兼汚水
流出用第1流水管5と濾水流入兼洗浄水流出用第2流水
管7との配管の所望部位をフレキシブルジョイント5
7、58としてある。符号59は吊り金具である。
As shown in FIGS. 1 and 4, at least one and preferably two rails 50 are provided on the outer periphery of the horizontal drum 3 and preferably a pair of guide grooves 51a for guiding the rails 50 are provided. The pair of guide groove rollers 51, 52 supported by rollers 51, 52 provided with a pair of guide grooves 52a, 52a are rotatably mounted on U-shaped frames 53, 54 by shafts 55, 56, and these frames are the rails described above. The base 50 is mounted on the base 19 by welding or the like so as to sandwich the base 50. Also, although not shown, the rails may be concave grooves and the rollers may be convex,
Hereinafter, the rail and the roller provided with the guide include both of the above. By supporting the drum 3 having such a horizontal play, the center of the rotating shaft of the drum can be easily set, and the total weight of the filter tank and the pipes is supported at the lower portion, so that the filter tank can be enlarged. A large-scale sewage treatment can be performed, a load on a cam floor or the like on a driving unit side can be reduced, a mechanism can be simplified, and a processing device with less trouble can be achieved. In addition, since the drum 3 having a play in front, rear, left and right is supported, a desired portion of the pipe between the first flowing water pipe 5 for raw water inflow and sewage outflow and the second flowing water pipe 7 for filtrate inflow and washing water outflow is connected to a flexible joint. 5
7, 58. Reference numeral 59 denotes a hanging bracket.

【0011】さらに、ドラム3の外からその軸心部を貫
通し原水流入兼汚水流出用第1流水部4が空間部2内に
位置している原水流入兼汚水流出用第1流水管5の取り
付け角度を、粒状濾材の上方で濾材の安定角よりドラム
の回転方向へ略90度の範囲内とした。好ましくは濾材
の安定角より60度(略真上)とするとよい。これによ
り、粒状濾材からなる濾槽1の逆洗時に粒状濾材が崩れ
始める安定角(粒状濾材の径、材質、回転速度等で異な
るが略30度)よりドラムの回転角が大きくなり、土砂
崩れのように粒状濾材が崩れ始めて濾材が巻き上って
も、流水管5が離れた位置なので、流水管5より粒状濾
材が流れ出ることを防止できる。さらにまた、原水流入
兼汚水流出用第1流水管又は濾水流入兼洗浄水流出用第
2流水管に、濾過時に原水流入又は処理水流出時に全開
となり、逆洗洗浄時に於いては洗浄汚水流出又は洗浄水
流入時に絞り開口となる弁を付設した、図5に示すよう
に、好ましくは濾水流入兼洗浄水流出用第2流水管7に
連通する側の配管に、弁筐60内に軸62により弁座6
6に対して開閉するバタフライ弁61が取り付けられ、
このバタフライ弁61には絞り孔63が穿設されてお
り、弁の取換え等のため弁筐60の上部に蓋64がボル
ト65により取り付けられている。このような弁によ
り、洗浄水(点線の矢印方向)の流れに対しては所望の
流量が自動的に得られ、処理された水(濾水の流れ方向
は実線の矢印方向)が流れ出る時には全開となり、かつ
ドラム内には圧が掛からないのでなんら不都合は生じな
い。
Further, a first flowing water section 4 for raw water inflow and sewage discharge which penetrates from the outside of the drum 3 and passes through the axial center thereof is located in the space section 2 of the first flowing water pipe 5 for raw water inflow and sewage discharge. The mounting angle was within a range of approximately 90 degrees in the rotation direction of the drum from the stable angle of the filter medium above the granular filter medium. Preferably, the angle is set to 60 degrees (substantially directly above) the stable angle of the filter medium. As a result, the rotation angle of the drum becomes larger than the stable angle at which the granular filter medium starts to collapse (about 30 degrees depending on the diameter, material, rotation speed, etc. of the granular filter medium) at the time of back washing of the filter tank 1 made of the granular filter medium. Even if the filter medium starts to collapse and the filter medium rolls up, since the flowing water pipe 5 is at a distant position, it is possible to prevent the granular filter medium from flowing out of the flowing water pipe 5. Furthermore, the raw water inflow and wastewater outflow first water pipe or the filtered water inflow and washing water outflow second water pipe are fully opened at the time of raw water inflow or treated water outflow at the time of filtration, and washed out at the time of backwashing and washing. Alternatively, as shown in FIG. 5, a valve, which is provided with a throttle opening when the washing water flows in, is preferably provided with a shaft in the valve housing 60 on a side communicating with the second drainage pipe 7 for inflow of filtration water and outflow of washing water. The valve seat 6 by 62
6, a butterfly valve 61 that opens and closes is attached,
A throttle hole 63 is formed in the butterfly valve 61, and a lid 64 is attached to an upper portion of the valve housing 60 by bolts 65 for replacing the valve. With such a valve, a desired flow rate is automatically obtained for the flow of the washing water (in the direction of the dotted line), and the valve is fully opened when the treated water (the flow direction of the filtrate is flowing in the direction of the solid line) flows out. , And no inconvenience occurs because no pressure is applied in the drum.

【0012】次ぎに、他の実施例を説明する、図6に示
すように、横型のドラム3にレール50、ローラ51等
を省略し、濾水流入兼洗浄水流出用第2流水部6と連通
させる濾水流入兼洗浄水流出用第2流水管7を横型のド
ラム3の他端に軸受け22と一体的に固定され、該軸受
け22と基台19の支持枠20上で、支持枠20に12
0度間隔に取付けた3個のカムフォロア(球面外輪)2
3…とにより横型のドラム3を回転自在に支持させてあ
る。さらに、他の実施例として、図7に示すように、前
記濾槽1内と空間部2内とには前記横型のドラム3と共
に回転し、濾槽1内では前記濾水流入兼洗浄水流出用第
2流水部6と連通する板状の濾過網8を付設し、空間部
2内では原水流入兼汚水流出用第1流水管4と連通する
板状の濾過網8を付設した汚水の処理装置である。この
ものは、上記図1、図6のものと同じ部位は同じ符号を
付し、その説明を省略する。そして、上述の各実施例の
前記原水流入兼汚水流出用第1流水管と、濾水流入兼洗
浄水流出用第2流水管とのいずれか一方又は両方が横型
のドラムの外に配設し、該配設が濾槽内に位置している
原水流入兼汚水流出用第1流水部又は濾水流入兼洗浄水
流出用第2流水部と連通させた汚水の処理装置である。
すなわち、濾槽を広くするとともに濾材の回転時に濾水
流入兼洗浄水流出用第2流水管7に当たり邪魔になると
いうことを防ぐために、例えば、図8に示すように、濾
水流入兼洗浄水流出用第2流水管7を横型のドラム3の
外部に配管してもよい。そして、板状の濾過網8を横型
のドラム3の全長幅の略全面に付設できるので、より一
層の濾過効率アップにつながる。さらに、原水流入兼汚
水流出用第1流水管4を横型のドラム3の外部に配管し
てもよい。このように濾槽1をドラム3内の全幅に広く
できるので濾過効率の向上が可能である。なお、図8、
図9に示したように、蓋とその内面に付設したウェッジ
ワイヤーの濾過網8とは横型のドラム3の曲面と一致さ
せてもよいし、濾過網8のみは偏平状や平面状としても
作用上差異は生じないので、以下、本願発明において
は、これらの曲面或いは偏平状や平面状とを板状とい
う。
Next, another embodiment will be described. As shown in FIG. 6, the rail 50, the rollers 51 and the like are omitted from the horizontal drum 3, and the second running water section 6 for inflow of drainage and outflow of washing water is provided. The second drain pipe 7 for inflow of drainage water and outflow of washing water to be communicated is integrally fixed to the other end of the horizontal drum 3 with the bearing 22, and on the support frame 20 of the bearing 22 and the base 19, To 12
Three cam followers (spherical outer ring) mounted at 0 degree intervals 2
3, the horizontal drum 3 is rotatably supported. Further, as another embodiment, as shown in FIG. 7, the inside of the filter tank 1 and the space 2 rotate together with the horizontal drum 3, and the inside of the filter tank 1 and the outflow of the washing water. Wastewater treatment provided with a plate-shaped filtration network 8 communicating with the second flowing water section 6 and a plate-shaped filtration network 8 communicating with the first flowing water pipe 4 for raw water inflow and sewage discharge in the space 2. Device. The same parts as those in FIGS. 1 and 6 are denoted by the same reference numerals, and description thereof will be omitted. Either one or both of the first flowing pipe for raw water inflow and sewage outflow and the second flowing water pipe for infiltration and washing water outflow in each of the above-described embodiments is disposed outside a horizontal drum. This arrangement is a sewage treatment apparatus in which the arrangement is connected to a first flowing section for raw water inflow and sewage outflow or a second flowing section for filtrate inflow and rinsing water outflow located in the filter tank.
That is, as shown in FIG. 8, for example, as shown in FIG. 8, in order to increase the size of the filter tank and to prevent the filter medium from rotating and obstructing the second flowing water pipe 7 for inflow of drainage and outflow of cleaning water, The second outflow water pipe 7 may be provided outside the horizontal drum 3. In addition, since the plate-shaped filtration net 8 can be provided over substantially the entire length of the horizontal drum 3, the filtration efficiency is further improved. Further, the first flush pipe 4 for raw water inflow and sewage outflow may be provided outside the horizontal drum 3. As described above, since the filter tank 1 can be widened to the entire width in the drum 3, the filtration efficiency can be improved. Note that FIG.
As shown in FIG. 9, the lid and the filter net 8 of the wedge wire attached to the inner surface thereof may be made to coincide with the curved surface of the horizontal drum 3, or only the filter net 8 may have a flat or planar shape. Since there is no difference, the curved surface, the flat shape, or the flat shape is hereinafter referred to as a plate shape in the present invention.

【0013】さらには、板状の濾過網8とドラム3の内
壁間にドラムの回転に追従する濾過網の裏面の清掃・藻
類等の付着物防止手段を設けた、この清掃・藻類等の付
着物手段は、図13乃至図17に示すように、好ましく
は一枚の金属製或いは合成樹脂製の板31に多数の合成
樹脂製或いは金属製のブラシ32を植設するか、また
は、連結棒33に対向する金属製或いは合成樹脂製の板
34に軸受管35を対象的にボルト・ナットや溶接或い
は接着して取り付け、対の合成樹脂製或いは金属製の羽
毛部を有する回転ブラシ36の合成樹脂製或いは金属製
の回転軸37の両端を差し込む、この回転ブラシの軸は
可撓性にして折り曲げその両端を軸受管の内径部38に
挿入する方が操作が簡単でよい。また、濾過網の裏面の
清掃・藻類等の付着物防止手段は、図示していないが、
発泡材に研磨剤を混入させた多数の塊とするとよい。こ
の塊の形状は好ましくは球状がよいが、球状に凹凸のあ
る塊や立方体や多面体でもよく、材質も金属、セラミッ
クス、或いはブラシを束ねたたわし、等でもよく、以下
本発明では単に多数の摺接塊という。さらに好ましくは
上述の全ての濾過網の裏面の清掃・藻類等の付着物防止
手段を好ましくは合成樹脂製の素材で構成し、防ばい剤
を混入或いは被覆させることで、長期の使用に際しても
これらの付着物防止手段に藻類等の付着物防止が可能と
なり、メンテナンスが楽な清潔で濾過効率の低下を防げ
るものである。そして、これらの防ばい剤として、高温
でも分解せず安全性が高い“商標サイアベンダゾール、
T、B、Z(米国メルク社製)、化学名「2(4−チア
ゾリルベンツミダゾール」”、或いは“商標バイナジン
(米国ベントロン社製)、化学名「10、10オキシフ
エノキシアルシン」”、“商標ノブコサイドN−96
(米国サンノブコ社製)”等がある。また、被覆剤とし
て、クロルヘキシジン及び銀塩からなる殺菌剤を一種類
以上を被覆、或いは微粒子状金属銅とロジン系樹脂をセ
ルローズ系高分子物質よりなる展着剤中に分散した組成
物でもよく、要するに付着物防止手段に混入或いは被覆
することでこれらの手段に藻類等の付着が防止できるも
のであればよいので、上述のものに限定されるものでは
なく、以下本発明では防ばい剤等を混入或いは被覆する
と表現する。板状の濾過網にも同様な防ばい剤等を混入
或いは被覆するとよい。なお、濾過網の全幅に対して、
2〜3個の上述の各ブラシが付設されるように、各ブラ
シの幅の寸法を決めればよいし、また、濾過網の裏面部
位に各ブラシの案内ガイドを付設したり、或いは板31
の両面にブラシ32…を植設しドラム3に接する面をド
ラムの形状に合わせた曲面としてもよい。また、板状の
ブラシの幅や回転ブラシの径も濾過網とドラムの内壁間
との間で自由に移動できる寸法にすればよい。さらに、
板状の濾過網をポリプロピレン等の合成樹脂製にして防
ばい剤等を混入させ、蓋に取り付ける場合は、蓋をも合
成樹脂製にして防ばい剤等を混入させると共に、この蓋
を透明にすれば内部の点検もできる、また、これらの濾
過網や蓋が金属製の場合は防ばい剤等を被覆すればよ
い。
Furthermore, a means for cleaning the back surface of the filter net following the rotation of the drum and preventing foreign matter such as algae between the plate-like filter net 8 and the inner wall of the drum 3 is provided. As shown in FIGS. 13 to 17, the kimono means preferably includes a plurality of synthetic resin or metal brushes 32 implanted on a single metal or synthetic resin plate 31 or a connecting rod. A bearing tube 35 is attached to a metal or synthetic resin plate 34 opposed to the bearing 33 by bolts and nuts or welded or adhered, and a rotating brush 36 having a pair of synthetic resin or metal feathers is synthesized. Both ends of the rotating shaft 37 made of resin or metal are inserted, and the shaft of the rotating brush is made flexible so that it is easier to operate by inserting both ends into the inner diameter portion 38 of the bearing tube. In addition, the means for cleaning the back surface of the filtration net and preventing foreign substances such as algae are not shown,
It is preferable to form a large number of lumps obtained by mixing an abrasive into a foam material. The shape of this lump is preferably spherical, but it may be a lump having irregularities in a spherical shape, a cube or a polyhedron, and the material may be metal, ceramics, or a bundle of brushes, and the like. It is called ingot. More preferably, the means for cleaning the back surface of all the above-mentioned filtration nets and preventing deposits such as algae are preferably made of a synthetic resin material, and mixed or covered with a deodorant, so that even when used for a long period of time, Thus, it is possible to prevent the attachment such as algae from being caused by the attachment prevention means, and to maintain the cleanliness easily and prevent a decrease in filtration efficiency. And, as these deterrents, "Trademark siabendazole," which is highly safe without decomposition even at high temperatures,
T, B, Z (manufactured by Merck, USA), chemical name "2 (4-thiazolylbenzmidazole)" or "trademark binazine (manufactured by Bentron, USA), chemical name" 10,10 oxyphenoxyarsine ""," Trademark Nobucoside N-96 "
(Manufactured by Sannobco, Inc., USA). As a coating agent, one or more bactericides consisting of chlorhexidine and a silver salt are coated, or fine metal copper and a rosin-based resin are coated with a cellulose-based polymer. The composition dispersed in the adhesive may be used. In other words, the composition is not limited to the above-described ones as long as it can prevent adhesion of algae or the like to these means by mixing or coating with the adhesion preventing means. In the following, the present invention will be described as mixing or covering a screening agent, etc. A similar screening agent or the like may be mixed or covered in a plate-like filtration net.
The width of each brush may be determined so that two or three brushes are provided, or a guide for each brush may be provided on the back surface of the filter net, or a plate 31 may be provided.
The brushes 32 may be implanted on both sides of the drum 3, and the surface in contact with the drum 3 may be a curved surface matching the shape of the drum. Also, the width of the plate-like brush and the diameter of the rotating brush may be set to a size that can freely move between the filtration net and the inner wall of the drum. further,
When the plate-shaped filter net is made of synthetic resin such as polypropylene and mixed with a protective agent, etc., and when it is attached to the lid, the lid is also made of synthetic resin and mixed with the protective agent, and the lid is made transparent. Then, the inside can be inspected. When these filtration nets and lids are made of metal, they may be covered with a deodorant or the like.

【0014】なお、濾過網8を付設し連通されている濾
水流入兼洗浄水流出用第2流水部6が下になるように横
型のドラム3の回転が停止されるよう、横型のドラム3
の所望位置に図示していないカムを設け、該カムと接触
するカムスイッチとで濾水流入兼洗浄水流出用第2流水
部6が下になるように横型のドラム3の回転が停止され
るになっている。この機構は濾水流入兼洗浄水流出用第
2流水部6が下になるような位置をセンサー(図示して
いない)で検知したり、回転する軸受け等の回転角をセ
ンサー(図示していない)で検知して、濾水流入兼洗浄
水流出用第2流水部6が下になるように横型のドラム3
の回転を停止させてもよい。さらにまた、図6に示すよ
うに、濾材がドラムの回転を支持する流水管の軸受部に
入込むのを防止するために、横型のドラム3の回転を支
持する軸心部として機能する原水流入兼汚水流出用第1
流水管5の内側に防砂パッキン70を装着してある。な
お、軸受け22と回動しなくかつ上記濾水流入兼洗浄水
流出用第2流水管7と連通し合う固定管24とは、ダス
トシール、グランドパッキング15、グランド押え等を
介して取付けられている、また、バルブコントロール2
5が配管上にとりつけられ後述の原水や洗浄水を選択的
に横型のドラム3内に給配する。符号26は原水入口、
符号27は処理水出口、符号28は排水出口である。
The horizontal drum 3 is provided with a filtration network 8 so that the rotation of the horizontal drum 3 is stopped so that the second drainage section 6 for inflow of drainage and outflow of washing water, which is in communication with the second drainage section 6, is downward.
The rotation of the horizontal drum 3 is stopped by a cam switch (not shown) provided at a desired position and a cam switch which comes into contact with the cam so that the second flushing section 6 for inflow of drainage and outflow of washing water is downward. It has become. This mechanism detects a position where the second flowing water part 6 for inflow of drainage and outflow of washing water is lowered by a sensor (not shown), and detects a rotation angle of a rotating bearing or the like (not shown). ), And the horizontal drum 3 is positioned so that the second flowing water portion 6 for inflow of filtered water and outflow of washing water is downward.
May be stopped. Further, as shown in FIG. 6, in order to prevent the filter medium from entering the bearing portion of the running water pipe supporting the rotation of the drum, the inflow of raw water that functions as an axis supporting the rotation of the horizontal drum 3 is performed. The first for sewage discharge
A sandproof packing 70 is mounted inside the water pipe 5. The fixed pipe 24 which does not rotate with the bearing 22 and communicates with the second flush pipe 7 for inflow of drainage and outflow of washing water is attached via a dust seal, a gland packing 15, a gland presser and the like. , And valve control 2
5 is mounted on the pipe, and supplies raw water and washing water to be described later selectively into the horizontal drum 3. Reference numeral 26 is a raw water inlet,
Reference numeral 27 denotes a treated water outlet, and reference numeral 28 denotes a drain outlet.

【0015】そして、処理装置において、原水は、図1
等中の実線矢印で示すように、濾槽静止状態で原水入口
26→管29→第1流水管5→第1流水部4→空間部2
→濾層表面→濾層1→略板状の濾過網8→第2流水部6
→第2流水管7を経て処理水出口28される。次ぎに、
処理装置の濾材洗浄作用について説明する。逆流水を使
用せずに濾槽を回転させ粒状濾材同志が擦り合わされ濾
材から付着物の剥離及び濾過網8の擦り合わせ洗浄が行
われる。ついで、洗浄水(処理水でもよい)をポンプ
(図示せず)の作動等により第2流水管7からドラム3
内に点線矢印のように継続的に流入されるようにすると
共に、ドラム3を駆動手段17〜19等で駆動させる。
それにより、ドラム3が回転して粒状濾材同志が擦り合
わされ、濾層1内の粒状濾材が安定角よりおおきくなる
と崩れだし、粒状濾材の付着物質を解離させ、かつ、粒
状濾材がドラム3内に付設された略板状の濾過網8とも
擦り合わされ、この略板状の濾過網8の付着物質をも解
離させ、これらは付着物質の解離時間内は通水しなくて
も行なえるのでさらに従来の濾過装置に比べて小容量の
洗浄水で洗浄できる。これらの解離した付着物質は、洗
浄水のながれである点線矢印で示すように、原水入口2
6→第2流水管7→第2流水部6→第2流水部6の略板
状の濾過網8→濾層1→濾層表面→空間部2→第1流水
部4→第1流水管5を経て外部に排水出口27される。
したがって、濾材洗浄は、粒状濾材がドラム3内に付設
された略板状の濾過網と擦り合わされ、この略板状の濾
過網の付着物質を解離させると共に、また粒状濾材同志
が擦り合わされ、粒状濾材の付着物質を解離させるの
と、濾層1内における第2流水部6からの洗浄水の流出
との相乗効果により略完壁に行われる。さらに、配管内
及び粒状濾材内部の付着物汚水を排出し、初期濾過水に
汚水が混入しないように、逆流洗浄後に濾槽静止状態で
順流水による残存付着物の槽外への除去をする洗浄工程
を行うとよい。次ぎに、これら各実施例の汚水処理装置
の使い方について説明すると、通常の濾過装置として所
定時間利用して、濾材を逆洗洗浄する際に、ドラムの外
周のレールとローラの支持で、或いはカムフォロアで横
型のドラムを回転させ、ドラムの内周面で濾材を崩落さ
せ、強制的に濾材同志と、濾材と略板状の濾過網とを擦
り合わして付着物質を解離させる。また、板状の濾過網
とドラムの内壁間にドラムの回転に追従する濾過網の清
掃・付着防止手段で好ましくは一枚の板に多数のブラシ
を植設したものか、対向する板に少なくとも1本の回転
ブラシを付設したもの或いは多数の摺接塊を濾過網とド
ラムの内壁間にいれておくだけで、濾過中はもちろん逆
洗時のドラムの回転にしたがつて該ブラシ等が濾過網の
裏面を摺動して汚れや藻類等の付着を防止すると共に汚
れ等が付着しても落としてくれるので水と共に外部に自
動的に排出できる。また、濾過時に原水流入又は処理水
流出時に全開となり逆洗洗浄時に洗浄汚水流出又は洗浄
水流入時に絞り開口となる弁を付設したので、流量の調
節を自動化し、洗浄水の大幅な節約を計った汚水処理装
置である。さらに、逆洗時の粒状濾材の崩落による濾材
の巻上げがあっても、流水管の開口が崩落よりより遠い
位置で濾材の巻上げに影響せず、かつ空気溜り部の濾材
はドラムの回転に追従してしまうので、流水管の開口よ
り粒状濾材の流出を略完全に防止できるのである。さら
には、防砂パッキンにより回転軸部から濾材の流出も防
止できる。
In the treatment apparatus, the raw water is supplied as shown in FIG.
As indicated by solid arrows in the drawings, the raw water inlet 26 → pipe 29 → first flowing water pipe 5 → first flowing water part 4 → space part 2 with the filter tank stationary.
→ Filter layer surface → Filter layer 1 → Substantially plate-shaped filtration network 8 → Second flowing water section 6
→ The treated water outlet 28 passes through the second flowing water pipe 7. Next,
The filter medium cleaning action of the processing device will be described. The filter tank is rotated without using the backflow water, and the granular filter media are rubbed against each other, so that the deposits are separated from the filter media and the filter net 8 is rubbed and washed. Next, washing water (which may be treated water) is supplied from the second flowing water pipe 7 to the drum 3 by operating a pump (not shown) or the like.
And the drum 3 is driven by driving means 17 to 19 and the like.
As a result, the drum 3 rotates and the granular filter media rub against each other. When the granular filter media in the filter layer 1 becomes larger than the stable angle, the granular filter media collapses to dissociate the adhered substances of the granular filter media, and the granular filter media enters the drum 3. It is also rubbed with the attached substantially plate-shaped filtration network 8 to dissociate the adhering substances of the substantially plate-shaped filtration net 8, which can be performed without passing water during the dissociation time of the adhering substances. It can be washed with a smaller volume of washing water than the filtration device of the above. These dissociated adhering substances are supplied to the raw water inlet 2 as shown by the dotted arrows indicating the flow of the washing water.
6 → second flowing water pipe 7 → second flowing water part 6 → substantially plate-shaped filtration network 8 of second flowing water part 6 → filter layer 1 → filter layer surface → space part 2 → first flowing water part 4 → first flowing water pipe Through 5, the water is discharged to the outside 27.
Therefore, in the filter medium washing, the granular filter medium is rubbed with the substantially plate-shaped filter net provided in the drum 3 to dissociate the adhering substances of the substantially plate-shaped filter network, and the granular filter medium is rubbed together to form a granular filter medium. The synergistic effect between the dissociation of the adhering substance of the filter medium and the outflow of the washing water from the second flowing water section 6 in the filter layer 1 is performed to a substantially complete wall. In addition, cleaning to discharge the adhering matter wastewater in the pipe and the inside of the particulate filter medium, and to remove the remaining adhering matter to the outside of the tank by the downstream water in the still state of the filter tank after the backflow washing so that the wastewater is not mixed into the initial filtration water. A step may be performed. Next, how to use the sewage treatment apparatus of each of the embodiments will be described. When the filter medium is used for a predetermined period of time as a normal filtration apparatus to backwash and wash the filter medium, it is supported by rails and rollers on the outer periphery of the drum or by a cam follower. Then, the horizontal drum is rotated to collapse the filter medium on the inner peripheral surface of the drum, and the filter medium is forcibly rubbed with the filter medium and the substantially plate-shaped filter net to dissociate the adhering substances. In addition, a cleaning / adhesion prevention means for the filter net following the rotation of the drum between the plate-shaped filter net and the inner wall of the drum is preferably one in which a large number of brushes are planted on one plate, or at least the opposite plate is provided. Simply put a rotating brush attached or a large number of sliding masses between the filter net and the inner wall of the drum. During the filtration, the brush etc. are filtered according to the rotation of the drum during backwashing. Sliding on the back side of the net prevents dirt and algae from adhering, and also removes dirt and the like, so that they can be automatically discharged to the outside together with water. In addition, a valve is provided that opens fully when raw water or treated water flows out during filtration and becomes a throttle opening when washing wastewater flows out or washing water flows in during backwashing. Wastewater treatment equipment. Furthermore, even if the filter medium is wound up due to the collapse of the granular filter medium during backwashing, the opening of the water pipe does not affect the winding up of the filter medium at a position farther than the collapse, and the filter medium in the air reservoir follows the rotation of the drum Therefore, it is possible to almost completely prevent the granular filter medium from flowing out from the opening of the water pipe. Furthermore, outflow of the filter medium from the rotating shaft can be prevented by the sandproof packing.

【0016】[0016]

【発明の効果】第1に、従来のような大規模な沈殿槽を
必要とせず、又は物理的濾過手段を採用することで大規
模な沈殿槽を小形化するか予備的ものとし、生物処理槽
をも大幅削減とし、物理的濾過ではできないとされてい
た汚水をPH調整して、不溶解性浮遊物質を発生させ、
該浮遊物質を簡単に物理的処理する汚水処理方法であ
る。第2に、従来のような大規模な沈殿槽を必要とせ
ず、又は物理的濾過手段を採用することで大規模な沈殿
槽を小形化するか予備的ものとし、生物処理槽をも大幅
削減とし、物理的濾過ではできないとされていた汚水を
消石灰等の金属石鹸でPH調整して、不溶解性浮遊物質
を発生させ、該浮遊物質を簡単に回転式で逆洗式濾過装
置により汚水処理する方法である。第3に、第1の効果
又は第2の効果に加えて、予備的沈殿槽と必要な規模の
生物処理槽と殺菌とで用水或いは中水として利用できる
汚水処理する方法である。第4に、浮遊物質等を濾過す
るに、濾過網の面積を拡げて濾過効率を上げるととも
に、逆洗時に濾材同志を擦り合せて、無理なく濾過網に
付着した汚物や懸濁物等を破壊し除去でき、かつ従来の
固定式で逆洗式濾過装置に比べて略1/10という少な
い洗浄水で濾材の洗浄が可能な処理装置なので、確実に
効率的に浮遊物質を回収できる汚水処理装置である。第
5に、第4の効果に加えて、濾槽内と空間部内とに板状
の濾過網を設けたので、濾過が荒い濾過と濾槽内の濾過
との二重濾過ができると共に、逆洗時にこれら板状の濾
過網に付着したものは自動的に洗浄してくれる汚水処理
装置である。第6に、第4又は第5の効果に加えて、原
水流入兼汚水流出用第1流水管と、濾水流入兼洗浄水流
出用第2流水管とのいずれか一方又は両方を横型のドラ
ムの外に配設したので、ドラム内にデットスペースを少
なく又は全くつくらないので、より小形化が可能とした
汚水処理装置である。第7に、第4乃至第6のいずれか
の効果に加えて、ドラムの内壁間に濾過時も濾過網の裏
面の自浄機能と藻類等の付着防止機能とを有すること
で、汚れや藻類等が付着したり、黴等が発生することを
防止すると共に汚れ等が付着してもドラムの回転により
自動的に洗浄してくれる処理装置なので、より確実に清
潔な汚水処理装置である。第8に、第7の効果に加え
て、付着物付着防止手段を防ばい剤を混入或いは被覆し
たことで、常に清潔に保てる汚水処理装置である。第9
に、第4乃至第8のいずれかの効果に加えて、濾過網に
防ばい剤を混入或いは被覆するだけで、濾過網の裏面の
清掃が長時間不要で藻類等の付着物防止がより確実にで
きる汚水処理装置である。第10に、第4乃至第9のい
ずれかの効果に加えて、原水流入兼汚水流出用第1流水
管又は濾水流入兼洗浄水流出用第2流水管に、原水流入
又は洗浄水流出時に全開となり汚水流出又は濾水流入時
に絞り開口となる弁を付設したので、流量の調節を自動
化し、洗浄水の節約を計った汚水処理装置である。第1
1に、第10の効果に加えて、弁の構造を簡単にすると
共に、浮遊物質の付着をも減らすことができる汚水処理
装置である。第12に、第4乃至第11のいずれかの効
果に加えて、原水流入兼汚水流出用第1流水管の取り付
け角度を、粒状濾材の静止時に対して90度乃至反回転
方向の安定角内としたので、逆洗時の粒状濾材の崩落に
よる濾材の巻上げがあっても、粒状濾材の流出を防止す
ることができる汚水処理装置である。第13に、第4乃
至第12のいずれかの効果に加えて、前記ドラムの外周
に少なくとも1条のレールを付設し、該レールを案内す
るガイドを設けたローラで支持したので、回転軸のセン
ターだしが楽にでき、濾過槽や配管等の総重量を下部で
支え、駆動部側のカムフロアー等の負担を軽減し、機構
を簡潔にでき、故障の少ない汚水の汚水処理装置であ
る。第14に、第4乃至第13のいずれかの効果に加え
て、濾材がドラムの回転を支持する流水管の軸受部に入
込むのを防止し、簡単な構造で、長期の使用に耐え、メ
ンテナンスの楽な耐久性がよい汚水処理装置である。
First, the biological treatment is not required because a large-scale sedimentation tank is not required, or a large-scale sedimentation tank can be reduced in size or made preliminary by employing a physical filtration means. The tank is also greatly reduced, and the pH of the sewage, which was considered impossible by physical filtration, is adjusted to generate insoluble suspended solids.
This is a sewage treatment method for simply physically treating the suspended matter. Secondly, the conventional large-scale sedimentation tank is not required, or the large-scale sedimentation tank is reduced in size or made preliminary by employing physical filtration means, and the biological treatment tank is also greatly reduced. The pH of sewage, which had been considered impossible by physical filtration, was adjusted with metal soap such as slaked lime to generate insoluble suspended solids. How to Third, in addition to the first effect or the second effect, there is a method of treating wastewater that can be used as service water or intermediate water in a preliminary sedimentation tank, a biological treatment tank of a required scale, and sterilization. Fourth, in order to filter suspended substances, the area of the filter net is increased to increase the filtration efficiency, and the filter media are rubbed together at the time of backwashing to easily destroy dirt and suspended matter adhering to the filter net. Sewage treatment equipment that can remove and remove suspended solids, and can efficiently and efficiently recover suspended solids, because it is a treatment equipment that can clean filter media with approximately 1/10 the amount of washing water compared to conventional fixed-type backwashing filtration equipment. It is. Fifth, in addition to the fourth effect, a plate-like filtration network is provided in the filter tank and in the space, so that double filtration of rough filtration and filtration in the filter tank can be performed. What adheres to these plate-shaped filtration nets at the time of washing is a sewage treatment apparatus that automatically cleans. Sixth, in addition to the fourth or fifth effect, one or both of a first flowing pipe for inflow of raw water and outflow of sewage and a second flowing pipe for inflow of filtered water and outflow of washing water are used as horizontal drums. The wastewater treatment apparatus has a small or no dead space in the drum because it is disposed outside the wastewater treatment apparatus. Seventh, in addition to the effects of any one of the fourth to sixth aspects, the filter has a self-cleaning function of the back surface of the filtration network and a function of preventing adhesion of algae and the like even when filtering between the inner walls of the drum, so that dirt, algae, etc. This is a processing device that prevents the generation of mold and mold and the like, and automatically cleans by rotating the drum even if dirt or the like adheres. Eighthly, in addition to the seventh effect, a sewage treatment apparatus that can always keep clean by mixing or covering an antifouling agent with an adhesion preventing means is provided. Ninth
Furthermore, in addition to the effects of any of the fourth to eighth aspects, only by mixing or covering the filter net with a deterrent agent, cleaning of the back surface of the filter net is not required for a long time, and the prevention of deposits such as algae is more reliable. It is a sewage treatment device that can be used. Tenth, in addition to the effects of any of the fourth to ninth effects, the first flow pipe for raw water inflow and sewage discharge or the second flow pipe for filtered water inflow and washing water outflow, This is a sewage treatment device that is fully opened and has a valve that becomes a throttle opening when sewage outflow or drainage inflow, so that flow rate adjustment is automated and washing water is saved. First
First, in addition to the tenth effect, the present invention is a sewage treatment apparatus capable of simplifying the structure of a valve and reducing adhesion of suspended substances. Twelfth, in addition to the effects of any one of the fourth to eleventh aspects, the angle of attachment of the first flush pipe for raw water inflow and sewage outflow is set within a range of 90 degrees to a stable angle in the anti-rotation direction with respect to the stationary state of the particulate filter medium. Therefore, the present invention is a sewage treatment apparatus capable of preventing the granular filter medium from flowing out even if the filter medium is wound up due to the collapse of the granular filter medium during backwashing. Thirteenth, in addition to the effects of any of the fourth to twelfth aspects, at least one rail is provided on the outer periphery of the drum, and the drum is supported by a roller provided with a guide for guiding the rail. This is a sewage treatment apparatus that can easily stock the center, support the total weight of the filtration tank and piping, etc. at the lower part, reduce the load on the cam floor and the like on the drive unit side, simplify the mechanism, and cause less trouble. Fourteenth, in addition to the effects of any of the fourth to thirteenth aspects, the filter medium is prevented from entering the bearing portion of the running water pipe that supports the rotation of the drum, has a simple structure, and can withstand long-term use. It is a sewage treatment device that is easy to maintain and has good durability.

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

【図1】本発明による汚水の処理装置の第1実施例を示
す断面図である。
FIG. 1 is a sectional view showing a first embodiment of a wastewater treatment apparatus according to the present invention.

【図2】本発明による汚水の処理装置の第1実施例を示
す平面図である。
FIG. 2 is a plan view showing a first embodiment of a wastewater treatment apparatus according to the present invention.

【図3】本発明による汚水の処理装置の第1実施例を示
す側面図である。
FIG. 3 is a side view showing a first embodiment of a wastewater treatment apparatus according to the present invention.

【図4】本発明による汚水の処理装置の第1図のA−A
線断面図である。
FIG. 4 AA of FIG. 1 of the wastewater treatment apparatus according to the present invention.
It is a line sectional view.

【図5】本発明による汚水の処理装置の要部の拡大図で
ある。
FIG. 5 is an enlarged view of a main part of the wastewater treatment apparatus according to the present invention.

【図6】本発明による汚水の処理装置の第2実施例を示
す断面図である。
FIG. 6 is a sectional view showing a second embodiment of the wastewater treatment apparatus according to the present invention.

【図7】本発明による汚水の処理装置の第3実施例を示
す断面図である。
FIG. 7 is a sectional view showing a third embodiment of the wastewater treatment apparatus according to the present invention.

【図8】本発明による汚水の処理装置の第4実施例を示
す断面図である。
FIG. 8 is a sectional view showing a fourth embodiment of the wastewater treatment apparatus according to the present invention.

【図9】本発明による板状の濾過網の一部拡大平面図で
ある。
FIG. 9 is a partially enlarged plan view of a plate-like filtration net according to the present invention.

【図10】本発明による図9の裏面一部拡大平面図であ
る。
FIG. 10 is a partially enlarged plan view of the back surface of FIG. 9 according to the present invention.

【図11】本発明による板状の濾過網を蓋の裏面に取り
付けた要部拡大平面図である。
FIG. 11 is an enlarged plan view of a main part in which a plate-shaped filtration net according to the present invention is attached to the back surface of a lid.

【図12】(イ)と(ロ)とは、本発明による板状の濾
過網の要部拡大平面図である。
FIGS. 12 (a) and (b) are enlarged plan views of essential parts of a plate-shaped filtration network according to the present invention.

【図13】本発明による濾過網の裏面の清掃・藻類等の
付着防止手段の拡大平面図である。
FIG. 13 is an enlarged plan view of a means for cleaning the back surface of the filter net and preventing adhesion of algae and the like according to the present invention.

【図14】本発明による図13の側面図である。FIG. 14 is a side view of FIG. 13 according to the present invention.

【図15】本発明による濾過網の裏面の清掃・藻類等の
付着防止手段の他の実施例の一部の平面図である。
FIG. 15 is a plan view of a part of another embodiment of the means for cleaning the back surface of the filter net and preventing adhesion of algae and the like according to the present invention.

【図16】本発明による図15の側面図である。FIG. 16 is a side view of FIG. 15 according to the present invention.

【図17】本発明による図15に使用されるブラシの側
面図である。
FIG. 17 is a side view of the brush used in FIG. 15 according to the present invention.

【符号の説明】[Explanation of symbols]

1 濾槽 2 空間部 3 横型のドラム 4 原水流入兼汚水流出用第1流水部 5 原水流入兼汚水流出用第1流水管 6 濾水流入兼洗浄水流出用第2流水部 7 濾水流入兼洗浄水流出用第2流水管 8 濾過網 9、64 蓋 10 フランジ 11、65 ボルト・ナット 13 ドラム(蓋)と濾過網との空間 14 ダストシール 15 グランドパッキング 16 軸受け部 17 スプロケット 18 モータ 19 基台 20、53、54 枠 21、23 カムフロアー 22 軸受け 24 固定管 25 5方バルブ 26 原水入口 27 処理水口 28 排水出口 31、34 板 32 ブラシ 33 連結棒 35 軸受管 36 回転ブラシ 37 回転軸 38 内径 50 レール 51、52 ローラ 55、56、62 軸 57、58 フレキシブルジョイント 59 吊り金具 60 弁筺 61 バタフライ弁 63 絞り孔 66 弁座 70 防水パッキン DESCRIPTION OF SYMBOLS 1 Filtration tank 2 Space part 3 Horizontal drum 4 First flowing water part for raw water inflow and sewage outflow 5 First flowing water pipe for raw water inflow and sewage outflow 6 Second flowing water part for filtered water inflow and washing water outflow 7 Filtration inflow Second water pipe for washing water outflow 8 Filtration net 9, 64 Lid 10 Flange 11, 65 Bolt / nut 13 Space between drum (lid) and filtration net 14 Dust seal 15 Ground packing 16 Bearing 17 Sprocket 18 Motor 19 Base 20 , 53, 54 Frame 21, 23 Cam floor 22 Bearing 24 Fixed pipe 25 Five-way valve 26 Raw water inlet 27 Treated water outlet 28 Drainage outlet 31, 34 Plate 32 Brush 33 Connecting rod 35 Bearing tube 36 Rotating brush 37 Rotating shaft 38 Inner diameter 50 Rail 51, 52 Roller 55, 56, 62 Shaft 57, 58 Flexible joint 59 Suspension fitting 60 Valve housing 61 Butterfly valve 63 Restriction hole 66 Valve seat 70 Waterproof packing

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B01D 33/58 C02F 1/50 550H C02F 1/50 510 560Z 520 B01D 23/24 C 33/18 A 550 33/36 560 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI B01D 33/58 C02F 1/50 550H C02F 1/50 510 560Z 520 B01D 23/24 C 33/18 A 550 33/36 560

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】汚水をPH調整して、不溶解性浮遊物質を
発生させ、該浮遊物質を逆洗式の物理濾過により処理し
たことを特徴とする汚水の処理方法。
1. A method for treating sewage, comprising adjusting the pH of sewage to generate insoluble suspended solids, and treating the suspended solids by backwashing physical filtration.
【請求項2】汚水を消石灰等の金属石鹸でPH調整し
て、不溶解性浮遊物質を発生させ、該浮遊物質を回転式
で逆洗式濾過手段により処理したことを特徴とする汚水
の処理方法。
2. The treatment of sewage, wherein the pH of the sewage is adjusted with a metallic soap such as slaked lime to generate insoluble suspended solids, and the suspended solids are treated by a rotary backwashing filtration means. Method.
【請求項3】汚水を沈殿槽に予備的に貯槽し、消石灰等
の金属石鹸でPH調整して、不溶解性浮遊物質を発生さ
せ、該浮遊物質を直接回転式で逆洗式濾過手段により処
理し、該処理水を必要に応じて生物処理槽で処理した後
に殺菌して用水或いは中水用水としたことを特徴とする
汚水の処理方法。
3. Preliminarily storing sewage in a sedimentation tank, adjusting the pH with a metal soap such as slaked lime to generate insoluble suspended solids, and directly rotating the suspended solids by backwashing filtration means. A method for treating sewage, comprising treating the treated water, treating the treated water in a biological treatment tank as necessary, and then sterilizing the treated water to use as tap water or tap water.
【請求項4】前記逆洗式濾過手段として、粒状濾材から
なる濾槽(1)と空間部(2)とが内部上下方向に形成
されている横型のドラム(3)と、この横型のドラム
(3)の外からその軸心部より原水流入兼汚水流出用第
1流水部(4)が空間部(2)内に位置している原水流
入兼汚水流出用第1流水管(5)と、前記横型のドラム
(3)の外からその軸心部より濾水流入兼洗浄水流出用
第2流水部(6)が濾槽(1)内に位置している濾水流
入兼洗浄水流出用第2流水管(7)とを有する濾過装置
において、 前記濾槽(1)内には前記横型のドラム(3)と共に回
転し、前記濾水流入兼洗浄水流出用第2流水部(6)と
連通する板状の濾過網(8)を付設したことを特徴とす
る汚水の処理装置。
4. A horizontal drum (3) in which a filter tank (1) made of a particulate filter medium and a space (2) are formed in the vertical direction as the backwashing filtration means, and a horizontal drum. From the outside of (3), a first flowing water section (4) for raw water inflow and sewage discharge from its axial center is located in the space (2) and a first flowing water pipe (5) for raw water inflow and sewage discharge. A second flushing section (6) for inflow of drainage and outflow of washing water from outside of the horizontal drum (3) is located in the filtration tank (1). In the filtration device having a second flowing water pipe (7), the filtration tank (1) rotates together with the horizontal drum (3), and the second flowing water section (6) for the inflow of filtered water and the outflow of washing water (6). ), Wherein a plate-like filtration network (8) communicating with the wastewater treatment apparatus is provided.
【請求項5】前記濾槽(1)内と空間部(2)内とには
前記横型のドラム(3)と共に回転し、濾槽(1)内で
は前記濾水流入兼洗浄水流出用第2流水部(6)と連通
する板状の濾過網(8)を付設し、空間部(2)内では
原水流入兼汚水流出用第1流水管(5)と連通する板状
の濾過網(8)を付設したことを特徴とする請求項4に
記載の汚水の処理装置。
5. The filter tank (1) and the space (2) rotate together with the horizontal drum (3) in the filter tank (1). 2 A plate-shaped filter net (8) communicating with the flowing water portion (6) is additionally provided, and a plate-shaped filtering net (5) communicating with the first flowing water pipe (5) for raw water inflow and sewage discharge in the space portion (2). The sewage treatment apparatus according to claim 4, further comprising (8).
【請求項6】前記原水流入兼汚水流出用第1流水管
(5)と、濾水流入兼洗浄水流出用第2流水管(7)と
のいずれか一方又は両方が横型のドラム(3)の外に配
設し、該配設が濾槽(1)内に位置している原水流入兼
汚水流出用第1流水部(4)又は濾水流入兼洗浄水流出
用第2流水部(6)と連通させたことを特徴とする請求
項4又は請求項5に記載の汚水の処理装置。
6. A drum (3) in which one or both of the first flowing pipe (5) for raw water inflow and sewage outflow and the second flowing water pipe (7) for inflow of filtered water and outflow of washing water are provided. And a second flowing section (6) for inflow of raw water and outflow of sewage or a second flowing section (6) for inflow of filtered water and outflow of washing water, which is located in the filter tank (1). The wastewater treatment device according to claim 4 or 5, wherein the wastewater treatment device is communicated with the wastewater treatment device.
【請求項7】前記濾槽(1)内には前記横型のドラム
(3)と共に回転し、前記濾水流入兼洗浄水流出用第2
流水部(6)と連通するウェッジワイヤー等の板状の濾
過網(8)を付設し、該板状の濾過網(8)とドラム
(3)の内壁間にドラムの回転に追従する濾過網の裏面
の清掃・藻類等のブラシ等の付着物防止手段を設けたこ
とを特徴とする請求項4乃至請求項6のいずれか1項に
記載の汚水の処理装置。
7. The filter tank (1) is rotated together with the horizontal drum (3) in the filter tank (1), so that the second filter for inflow of filtrate and outflow of washing water.
A filter net (8), such as a wedge wire, which is in communication with the flowing water section (6) is provided, and the filter net follows the rotation of the drum between the filter net (8) and the inner wall of the drum (3). The sewage treatment apparatus according to any one of claims 4 to 6, further comprising: means for cleaning the back surface of the sewage and preventing deposits such as brushes for algae.
【請求項8】前記清掃・藻類等の付着物防止手段に防ば
い剤等を混入或いは被覆したことを特徴とする請求項7
に記載の汚水の処理装置。
8. The cleaning / adhering substance preventing means such as algae is mixed or covered with a deodorizing agent or the like.
A wastewater treatment apparatus according to claim 1.
【請求項9】前記板状の濾過網(8)に防ばい剤等を混
入或いは被覆したことを特徴とする請求項4乃至請求項
8のいずれか1項に記載の汚水の処理装置。
9. The sewage treatment apparatus according to claim 4, wherein an anti-blocking agent or the like is mixed in or covered with the plate-shaped filtration network.
【請求項10】前記原水流入兼汚水流出用第1流水管
(5)又は濾水流入兼洗浄水流出用第2流水管(7)
に、原水及び洗浄水流入又は処理水及び洗浄水流出時に
全開となり汚水流出又は洗浄水流入時に絞り開口となる
弁(61)を付設したことを特徴とする請求項4乃至請
求項9のいずれか1項に記載の汚水の処理装置。
10. A first flowing pipe (5) for inflow of raw water and outflow of sewage or a second flowing pipe (7) for inflow of filtered water and outflow of washing water.
10. A valve according to claim 4, further comprising a valve (61) which is fully opened when the raw water and the wash water flows in or the treated water and the wash water flows out, and becomes a throttle opening when the waste water flows out or the wash water flows. The sewage treatment apparatus according to claim 1.
【請求項11】前記弁は、バタフライ弁(61)に所望
の径の孔(63)を穿設し、原水及び洗浄水流入又は処
理水及び洗浄水流出時の全開時はバタフライ弁として機
能し、汚水流出又は洗浄水流入時の絞り開口時には所望
の径の孔(63)による少流量として機能させたことを
特徴とする請求項10に記載の汚水の処理装置。
11. The valve has a butterfly valve (61) having a hole (63) of a desired diameter, and functions as a butterfly valve when the raw water and washing water are inflow or the treated water and washing water are fully opened. 11. The sewage treatment apparatus according to claim 10, wherein a small flow rate is provided by a hole (63) having a desired diameter at the time of opening the throttle at the time of sewage outflow or washing water inflow.
【請求項12】前記原水流入兼汚水流出用第1流水管
(5)の取り付け角度を、粒状濾材の上方で濾材の安定
角よりドラムの回転方向へ略90度の範囲内としたこと
を特徴とする請求項4乃至請求項11のいずれか1項に
記載の汚水の処理装置。
12. The installation angle of the first flowing water pipe (5) for inflow of raw water and outflow of sewage is within a range of about 90 degrees in the rotation direction of the drum from the stable angle of the filter medium above the granular filter medium. The sewage treatment apparatus according to any one of claims 4 to 11, wherein:
【請求項13】前記ドラムの外周に少なくとも1条のレ
ール(50)を付設し、該レールを案内するガイドを設
けたローラ(52)で支持したことを特徴とする請求項
4乃至請求項12のいずれか1項に記載の汚水の処理装
置。
13. The drum according to claim 4, wherein at least one rail (50) is provided on the outer periphery of said drum, and supported by rollers (52) provided with guides for guiding said rail. The sewage treatment apparatus according to any one of the above.
【請求項14】前記横型のドラムの回転を支持する軸心
部として機能する原水流入兼汚水流出用第1流水管
(5)の内側に防砂パッキン(70)を装着したことを
特徴とする請求項4乃至請求項13のいずれか1項に記
載の汚水の処理装置。
14. A sandproof packing (70) is mounted inside a first flow pipe (5) for raw water inflow and sewage discharge, which functions as an axis supporting the rotation of the horizontal drum. The sewage treatment apparatus according to any one of claims 4 to 13.
JP9114124A 1997-03-28 1997-03-28 Treatment of sewage and its treating device Pending JPH10272493A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9114124A JPH10272493A (en) 1997-03-28 1997-03-28 Treatment of sewage and its treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9114124A JPH10272493A (en) 1997-03-28 1997-03-28 Treatment of sewage and its treating device

Publications (1)

Publication Number Publication Date
JPH10272493A true JPH10272493A (en) 1998-10-13

Family

ID=14629745

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9114124A Pending JPH10272493A (en) 1997-03-28 1997-03-28 Treatment of sewage and its treating device

Country Status (1)

Country Link
JP (1) JPH10272493A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001058108A (en) * 1999-07-13 2001-03-06 Roumen Kaltchev Cleaner for liquid containing suspended substance
WO2002028503A1 (en) * 2000-09-29 2002-04-11 Takara Kogyo Kabusiki Kaisha Filter medium washing method and filter
JP2011098309A (en) * 2009-11-09 2011-05-19 Daido Machines Co Ltd Strainer element and filter using the same
JP5993480B1 (en) * 2015-03-30 2016-09-14 タカラ工業株式会社 Filtration device
CN109804964A (en) * 2019-02-19 2019-05-28 刘兆奇 Self-purging equipment and fish jar
KR20210105590A (en) * 2020-02-19 2021-08-27 장한기술 주식회사 High precision filtration device by adjusting the vortex strength

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001058108A (en) * 1999-07-13 2001-03-06 Roumen Kaltchev Cleaner for liquid containing suspended substance
WO2002028503A1 (en) * 2000-09-29 2002-04-11 Takara Kogyo Kabusiki Kaisha Filter medium washing method and filter
EP1329251A1 (en) * 2000-09-29 2003-07-23 Takara Kogyo Kabusiki Kaisha Filter medium washing method and filter
JPWO2002028503A1 (en) * 2000-09-29 2004-02-19 タカラ工業株式会社 Filter media cleaning method and filtration device
EP1329251A4 (en) * 2000-09-29 2004-10-06 Takara Thermistor Instr Filter medium washing method and filter
JP4609622B2 (en) * 2000-09-29 2011-01-12 タカラ工業株式会社 Filtration device
JP2011098309A (en) * 2009-11-09 2011-05-19 Daido Machines Co Ltd Strainer element and filter using the same
JP5993480B1 (en) * 2015-03-30 2016-09-14 タカラ工業株式会社 Filtration device
CN109804964A (en) * 2019-02-19 2019-05-28 刘兆奇 Self-purging equipment and fish jar
KR20210105590A (en) * 2020-02-19 2021-08-27 장한기술 주식회사 High precision filtration device by adjusting the vortex strength

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