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JP7576902B2 - Container-type trickling filter device and method for cleaning treated water tank in container-type trickling filter device - Google Patents
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JP7576902B2 - Container-type trickling filter device and method for cleaning treated water tank in container-type trickling filter device - Google Patents

Container-type trickling filter device and method for cleaning treated water tank in container-type trickling filter device Download PDF

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JP7576902B2
JP7576902B2 JP2022029104A JP2022029104A JP7576902B2 JP 7576902 B2 JP7576902 B2 JP 7576902B2 JP 2022029104 A JP2022029104 A JP 2022029104A JP 2022029104 A JP2022029104 A JP 2022029104A JP 7576902 B2 JP7576902 B2 JP 7576902B2
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JP2023125144A (en
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孝 松枝
晃弘 長野
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Sanki Engineering Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/04Aerobic processes using trickle filters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Description

本発明は、産業廃水、上下水、河川水などの汚水を浄化する汚水浄化装置における散水ろ床装置に関し、より詳細には反応槽内にろ材塊(微生物保持担体)を積層状に堆積させた散水ろ床にて微生物を付着させ、該散水ろ床の上から汚水を散布し、浸透流下した処理水を処理水槽外へ取り出すコンテナ型散水ろ床装置及びコンテナ型散水ろ床装置における処理水槽の洗浄方法に関する。 The present invention relates to a trickling filter device in a wastewater purification system that purifies wastewater such as industrial wastewater, water supply and sewage, and river water. More specifically, the present invention relates to a container-type trickling filter device in which microorganisms are attached to a trickling filter bed in which filter media blocks (microorganism-holding carriers) are stacked in layers in a reaction tank, wastewater is sprayed over the trickling filter bed, and the treated water that has permeated and flowed down is removed from the treated water tank, and a method for cleaning the treated water tank in a container-type trickling filter device.

汚水の浄化手法の一つとして、散水ろ床装置は古くから利用されている。
一般的な散水ろ床装置は、反応槽と該反応槽の上方部に設けられた散水装置と、反応槽を通った処理水を受けて溜める処理水槽とから構成され、前記反応槽内には汚水に含まれる微生物を付着させる微生物保持担体が充填され、この微生物保持担体の集合体で散水ろ床が形成されている。
汚水は上から散水され、反応槽内を重力で上から下に順番に流れて行き、その間に微生物保持担体により浄化されて処理された水は、下にある処理水槽に落ち溜まって行く。
このような散水ろ床装置は、電力消費が少なく、運転管理が容易で、汚泥発生量も少ないという長所がある。
Trickling filters have long been used as a method for purifying wastewater.
A typical trickling filter device is composed of a reaction tank, a trickling device installed above the reaction tank, and a treated water tank that receives and stores the treated water that has passed through the reaction tank.The reaction tank is filled with microorganism-retaining carriers to which microorganisms contained in the wastewater are attached, and the collection of these microorganism-retaining carriers forms a trickling filter bed.
Wastewater is sprayed from above and flows from top to bottom within the reaction tank due to gravity. During this time, the water is purified and treated by the microorganism retention carriers and falls into the treatment tank below.
Such a trickling filter has the advantages of low power consumption, easy operation and management, and low sludge production.

上記汚水浄化装置における微生物保持担体の一例として出願人は、反応槽の中にスポンジ担体を充填し処理水を降らせ(散水する)、前記スポンジ担体の周りに有る空気を取り込んで、担体の中にいる微生物が、その空気を利用して汚水中の有機物やアンモニアを酸化し、汚水を浄化する構成の水浄化装置を出願している(特開2019―171237号公報)。 As an example of a microorganism-holding carrier in the above-mentioned wastewater purification device, the applicant has applied for a water purification device configured to fill a reaction tank with sponge carriers, rain (sprinkle) treated water, take in air around the sponge carriers, and have the microorganisms in the carriers use the air to oxidize organic matter and ammonia in the wastewater, thereby purifying the wastewater (JP Patent Publication No. 2019-171237).

なお、散水ろ床装置が設置される場所によっては、チョウバエ等の虫が発生するので装置は囲われていて、装置の中を換気するような形でファンにより中に空気を供給している。一般的な構造では、反応槽(20)の下からファンで空気を吸い込んで換気している。これにより汚水の匂いが装置内に収容されている散水ろ床から直接漏れないように処理している。
前記処理水槽には、処理された水と同時に散水ろ床で捕捉しきれなかった固形物も落ちてくるが、処理水槽の中にこの固形物が落ちて水槽の中に長い間溜まってしまうと、それが腐敗して処理水を汚すので、その固形物を排出しなければいけない。
従来の散水ろ床装置においては、散水ろ床の下にある処理水槽の容積は大きく深さも十分あり、ある程度固形物を溜めて、処理水槽底部を固形物の排出を促すために20%程度の勾配をつけ、処理水槽底部付近に位置する固形物引き抜き管で溜った固形物を排出していた。また、スクレーパのある掻き寄せ機等で掻き集めて、ある程度固形物が溜まった時に排出することも行われる。
Depending on the location where the trickling filter device is installed, insects such as moth flies may appear, so the device is enclosed and air is supplied to the inside of the device by a fan to ventilate the inside. In a general structure, air is sucked in by a fan from below the reaction tank (20) to ventilate the inside of the device. This prevents the smell of wastewater from leaking directly from the trickling filter contained inside the device.
At the same time as the treated water, solid matter that has not been captured by the trickling filter falls into the treatment tank. If these solid matter falls into the treatment tank and remains there for a long time, it will rot and pollute the treated water, so the solid matter must be discharged.
In conventional trickling filter devices, the treated water tank below the trickling filter has a large volume and sufficient depth, and a certain amount of solid matter is accumulated, and the bottom of the treated water tank is sloped at about 20% to promote the discharge of solid matter, and the accumulated solid matter is discharged through a solid matter extraction pipe located near the bottom of the treated water tank.In addition, the solid matter is also scraped up with a scraper with a scraper, and discharged when a certain amount of solid matter has accumulated.

特開2019―171237号公報JP 2019-171237 A

電力消費が少なく、運転管理が容易で、汚泥発生量も少ないという長所がある散水ろ床装置は、後進国や開発途上国において環境汚染問題が深刻化するにあたって、その普及が期待されている。普及の手段として、散水ろ床装置を海上輸送用コンテナ内に組み込んで輸出することが考えられる。コンテナ型散水ろ床装置を国内工場で製作しておき、現地へ海上輸送し、据え付けて汚水や処理水等の配管の接続工事を行えば、迅速に使用が可能となる。
ところで、海上輸送用コンテナには寸法の規制があり、装置を寸法の規制内にする必要がある。一方で、汚水の浄化に寄与する散水ろ床の微生物量を十分に確保するために、散水ろ床の容量を十分に確保することが重要である。また、前述のとおり、従来の散水ろ床装置においては、散水ろ床下部の処理槽の容積は大きく深さも十分あるが、寸法規制のある海上輸送用コンテナに散水ろ床装置を組み込むには、処理水槽底部の勾配を固形物の排出を促すために十分確保できない。排出が促されなければ固形物の腐敗による悪臭の発生対策が必要となる。さらに、従来の掻き寄せ機を設ける場合には駆動装置等の補機スペースを確保しなければならない。
Trickling bed devices, which have the advantages of low power consumption, easy operation and management, and low sludge generation, are expected to become more widespread in developing countries as environmental pollution problems become more serious. One possible way to popularize them is to incorporate them into marine transport containers and export them. Container-type trickling bed devices can be manufactured in domestic factories, transported by sea to the site, installed, and connected to pipes for wastewater, treated water, etc., so that they can be used quickly.
However, there are size restrictions for marine transport containers, and the device must be within the size restrictions. On the other hand, it is important to ensure a sufficient capacity of the trickling filter in order to ensure a sufficient amount of microorganisms in the trickling filter that contributes to the purification of wastewater. As mentioned above, in conventional trickling filter devices, the treatment tank below the trickling filter is large in volume and deep enough, but in order to incorporate the trickling filter device into a marine transport container with size restrictions, the slope of the bottom of the treatment tank cannot be sufficiently ensured to promote the discharge of solids. If the discharge is not promoted, measures to prevent the generation of bad odors due to the decay of solids are necessary. Furthermore, when a conventional scraper is installed, space for auxiliary equipment such as a drive unit must be secured.

本発明は、上記の課題に鑑みてなされたものであり、散水ろ床装置において、散水ろ床下部の処理槽内に溜まった固形物を掻き寄せ機械等を使わずに自動的に排出することができ、かつ、寸法規制のある海上輸送用コンテナに組み込まれた散水ろ床装置を提供することを目的とする。
The present invention has been made in consideration of the above-mentioned problems, and has an object to provide a trickling filter device that can automatically discharge solids accumulated in the treatment tank below the trickling filter without using a scraping machine or the like, and that can be incorporated into a sea transport container which is subject to dimensional regulations.

本発明者は上記課題を下記の手段より解決した。
〔1〕反応槽(20)と反応槽(20)の内部を点検する点検口(27)と処理水槽(30)とからなる散水ろ床装置(1)であって、前記反応槽(20)は、気密性を備えた直方体からなる筐体(21)と、該筐体(21)の底部設けられたメッシュ状の底板(22)と、前記該筐体(21)内に充填された担体(23)とからなり、前記処理水槽(30)は、処理水の排出方向に向かって少なくとも1/100~15/100の勾配を設けている傾斜した長方形の底板(31)と、側壁(32~35)とからなる箱状体の本体(30A)と、
当該本体(30A)の処理水排出方向に設けられた水槽部(36)と、当該水槽部(36)に設けられた堰(37)と、空気引き抜き管(38)と、処理水引き抜き管(40)と、固形物引き抜き管(41)からなり、かつ前記水槽部(36)は散水ろ床装置(1)より水平方向の外側になるように構成されている
ことを特徴とするコンテナ型散水ろ床装置。
〔2〕前記水槽部(36)に循環用処理水引き抜き管(42)を設けたことを特徴とする〔1〕記載のコンテナ型散水ろ床装置。
〔3〕前記処理水槽(30)内に越流トラフ(43)を設け、当該越流トラフ(43)につながっている処理水引き抜き管(40)と循環用処理水引き抜き管(42)の間に隔て板(44)を移動可能に設けたこと特徴とする〔2〕に記載のコンテナ型散水ろ床装置。
〔4〕前記空気引き抜き管(38)の途中に、該空気引き抜き管(38)内から水溜まりを排出するドレン管(45)を設けたことを特徴とする〔1〕から〔3〕の何れか1に記載のコンテナ型散水ろ床装置。
〔5〕前記空気引き抜き管(38)を当該空気引き抜き管(38)の先端(38a)が下となるように傾斜をつけていることを特徴とする〔1〕から〔4〕何れか1に記載のコンテナ型散水ろ床装置。
〕前記散水ろ床装置(1)の前記処理水槽(30)を土木躯体とし、海上輸送用コンテナの寸法規制内で、前記処理水槽(30)が占めていたスペースを、前記散水ろ床装置(1)の前記反応槽(20)の容量に置き換えて増やすことを特徴とする〔1〕から〔〕の何れか1に記載のコンテナ型散水ろ床装置。
〔7〕前記反応槽(20)を複数段の前記筐体(21)で構成し、当該筐体(21)の個数を変えることで前記散水ろ床装置(1)の高さや、容積を変更することを特徴とする〔〕に記載のコンテナ型散水ろ床装置。
〔8〕固形物引き抜きを行う際には処理水槽(30)に溜まった処理水全量を固形物引き抜き管(41)の弁を開放して排出させたうえで、汚水を散水ろ床に散水させたまま、ろ床を通過して処理水槽(30)に滴下する処理水をシャワリングさせて底板(31)上にある溜った固形物を処理水とともに水平に近い緩い傾斜でも堰(37)方向に向かって送ることを特徴とする〔1〕から〔〕の何れか1に記載のコンテナ型散水ろ床装置の処理水槽(30)の洗浄方法。
The present inventors have achieved the above object by the following means.
[1] A trickling filter device (1) comprising a reaction tank (20), an inspection hatch (27) for inspecting the inside of the reaction tank (20), and a treated water tank (30), wherein the reaction tank (20) comprises an airtight rectangular parallelepiped housing (21), a mesh-like bottom plate (22) provided at the bottom of the housing (21), and a carrier (23) filled in the housing (21), and the treated water tank (30) comprises a box-shaped main body (30A) comprising an inclined rectangular bottom plate (31) having a gradient of at least 1/100 to 15/100 toward the discharge direction of the treated water, and side walls (32 to 35);
The system comprises a water tank section (36) provided in the treated water discharge direction of the main body (30A), a weir (37) provided in the water tank section (36), an air withdrawal pipe (38), a treated water withdrawal pipe (40), and a solid matter withdrawal pipe (41), and the water tank section (36) is configured to be horizontally outward of the trickling filter bed device (1).
A container-type trickling filter device characterized by the above.
[2] The container-type trickling filter apparatus according to [1], characterized in that a circulating treated water withdrawal pipe (42) is provided in the water tank section (36).
[3] A container-type trickling filter device as described in [2], characterized in that an overflow trough (43) is provided in the treated water tank (30), and a partition plate (44) is movably provided between the treated water withdrawal pipe (40) connected to the overflow trough (43) and the circulating treated water withdrawal pipe (42).
[4] A container-type trickling filter device as described in any one of [1] to [3], characterized in that a drain pipe (45) for discharging accumulated water from within the air extraction pipe (38) is provided midway through the air extraction pipe (38).
[5] A container-type trickling filter device described in any one of [1] to [4], characterized in that the air extraction pipe (38) is inclined so that the tip (38a) of the air extraction pipe (38) is downward.
[ 6 ] A container-type trickling filter device as described in any one of [1] to [5], characterized in that the treated water tank (30) of the trickling filter device (1) is used as a civil engineering structure, and the space occupied by the treated water tank (30) is replaced with and increased in capacity by the reaction tank ( 20 ) of the trickling filter device (1) within the dimensional regulations of marine transport containers.
[7] The container-type trickling bed device described in [6], characterized in that the reaction tank ( 20 ) is composed of multiple stages of the housings (21), and the height and volume of the trickling bed device (1) can be changed by changing the number of the housings (21).
[8] A method for cleaning the treated water tank (30) of a container-type trickling filter bed apparatus described in any one of [1] to [7], characterized in that when removing solids, the valve of the solids removal pipe (41) is opened to discharge the entire amount of treated water accumulated in the treated water tank (30), and while the wastewater is being sprayed onto the trickling filter bed, the treated water that passes through the filter bed and drips into the treated water tank (30) is showered to send the accumulated solids on the bottom plate ( 31 ) together with the treated water toward the weir (37) even at a gentle incline close to horizontal.

上記構成の本発明によれば、コンテナ型散水ろ床装置において、処理槽内に溜まった固形物を機械等を使わずに自動的に排出することができ、かつ、寸法規制のある海上輸送用コンテナに組み込まれた散水ろ床装置を提供することができる。 According to the present invention configured as above, in a container-type trickling filter device, it is possible to automatically discharge solids accumulated in the treatment tank without using machinery, etc., and to provide a trickling filter device that is incorporated in a sea transport container that is subject to dimensional regulations.

本発明のコンテナ型散水ろ床装置の実施例を側面から見た斜視図である。FIG. 1 is a perspective side view of an embodiment of a container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の実施例の正面図である。FIG. 2 is a front view of an embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の実施例の平面図である。FIG. 2 is a plan view of an embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の実施例の側面図である。FIG. 2 is a side view of an embodiment of the container-type trickling filter device of the present invention. 図3のA-A断面図AA cross-sectional view of FIG. 図4のB-B断面図BB cross-sectional view of FIG. 図4のC-C断面図4C-C cross-sectional view of FIG. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention. 本発明のコンテナ型散水ろ床装置の他の実施例を表す図FIG. 1 is a diagram showing another embodiment of the container-type trickling filter device of the present invention.

本発明を実施するための形態を、実施例の図に基づいて説明する。
図1は本発明のコンテナ型散水ろ床装置の実施例を側面から見た斜視図であり、外枠として海上輸送用コンテナを利用した例、図2は本発明のコンテナ型散水ろ床装置の実施例の正面図、図3は本発明のコンテナ型散水ろ床装置の実施例の平面図、図4は本発明のコンテナ型散水ろ床装置の実施例の側面図、図5は図3のA-A断面図、図6は、図4のB-B断面図、図7は図4のC-C断面図、図8、図9は本発明のコンテナ型散水ろ床装置の他の実施例を表す図である。
図1~図11において、1は散水ろ床装置であり、20は反応槽、30は処理水槽である。
本発明の実施例においては、コンテナ型散水ろ床装置の海上輸送を考慮し、海上輸送用コンテナの枠(51~54)を利用しているが、これに限定されるものではなく、本発明の特徴は、処理水槽30を小型化するとともに、掻き寄せ機等の機械を用いることなく処理水及び固形物を排出することができるコンテナ型散水ろ床装置にある。
反応槽20は、気密性を備えた直方体からなる筐体21からなり、該筐体21の底部には水平方向に沿ってメッシュ状の底板22が設けられている。
そして、該底板22の上には、連続気泡構造の多孔質体であり、保水性と柔軟性を備えた素材により形成されたスポンジ担体23(本発明において、担体23と称する場合もある。)が充填されている。
図11に示すように、本実施例の場合、前記スポンジ担体23は、微生物の付着する間隙を有する多孔体24と、該多孔体24を収容する枠体25により構成されている。
前記多孔体24の素材としては、具体的には、例えばウレタン樹脂、エステル重合体、エーテル重合体といった樹脂を発泡させた多孔質体が用いられる。
筐体21内のスポンジ担体23に対し、散水ろ床装置の上部に設けられた散水ノズル(図示せず)から汚水が散水される。当該散水された汚水は、スポンジ担体23の多孔体24に浸透したり、多孔体24の表面を通ったりして下方へ移動し、その間に汚水は多孔体24に付着した微生物によって浄化され処理水として散水ろ床の下方から滴下する。
このとき、枠体25に設けられた開口部25aから多孔体24の内部に浸透することになり、多孔体24の内部に存在する微生物に対し、液中の汚濁物質や担体間の間隙に供給される空気から液に溶存していく酸素等が効率良く供給され、汚水が浄化される。
26は、配管を接続するスペースと装置上部のほうへ移動して点検作業に使用する梯子であり、27は反応槽内部を点検するための点検口である。
なお、後述するように処理水槽30に設けられた空気引き抜き管38から、処理水槽30内の空気をファン等(図示せず)で引き込むと、前記反応槽20の筐体21内のスポンジ担体23の表面から酸素が溶け込んだ液が浸透して、前記反応槽20の筐体21内のスポンジ担体23に対して酸素等を供給するように運転されている。なお、ここでは担体の好適な例としてスポンジを取り上げたが、必ずしも多孔体24の素材としてスポンジを用いた担体23を用いる必要はない。例えば、担体23に代わりうるものとして、一般に水処理用ろ材として利用される石材や硬質樹脂等を用いることでもよい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the accompanying drawings.
FIG. 1 is an oblique side view of an embodiment of a container-type trickling filter bed device of the present invention, an example in which a marine transport container is used as the outer frame, FIG. 2 is a front view of an embodiment of a container-type trickling filter bed device of the present invention, FIG. 3 is a plan view of an embodiment of a container-type trickling filter bed device of the present invention, FIG. 4 is a side view of an embodiment of a container-type trickling filter bed device of the present invention, FIG. 5 is a cross-sectional view A-A of FIG. 3, FIG. 6 is a cross-sectional view B-B of FIG. 4, FIG. 7 is a cross-sectional view C-C of FIG. 4, and FIGS. 8 and 9 are diagrams showing other embodiments of a container-type trickling filter bed device of the present invention.
In Figures 1 to 11, reference numeral 1 denotes a trickling filter device, 20 denotes a reaction tank, and 30 denotes a treated water tank.
In the embodiment of the present invention, the frames (51-54) of containers for marine transport are used in consideration of the marine transportation of the container-type trickling filter device, but the present invention is not limited to this. A feature of the present invention is that the container-type trickling filter device can reduce the size of the treated water tank 30 and discharge treated water and solids without using machinery such as a scraper.
The reaction tank 20 is made of an airtight rectangular parallelepiped housing 21, and a mesh-like bottom plate 22 is provided on the bottom of the housing 21 along the horizontal direction.
A sponge carrier 23 (sometimes referred to as carrier 23 in the present invention) is filled on top of the bottom plate 22 and is made of a porous material with an open-cell structure that has water retention and flexibility.
As shown in FIG. 11, in this embodiment, the sponge carrier 23 is composed of a porous body 24 having gaps to which microorganisms can adhere, and a frame 25 for housing the porous body 24.
Specifically, the material for the porous body 24 is a porous body obtained by foaming a resin such as a urethane resin, an ester polymer, or an ether polymer.
Wastewater is sprayed from a spray nozzle (not shown) provided at the top of the trickling filter device onto the sponge carrier 23 inside the housing 21. The sprayed wastewater moves downward by penetrating the porous body 24 of the sponge carrier 23 or passing over the surface of the porous body 24, during which the wastewater is purified by the microorganisms attached to the porous body 24 and drips from the bottom of the trickling filter as treated water.
At this time, the liquid penetrates into the porous body 24 through the openings 25a provided in the frame 25, and oxygen and other substances dissolved in the liquid from the pollutants in the liquid and the air supplied to the gaps between the carriers are efficiently supplied to the microorganisms present inside the porous body 24, thereby purifying the wastewater.
Reference numeral 26 denotes a space for connecting pipes and a ladder used for moving to the top of the equipment for inspection work, and reference numeral 27 denotes an inspection hatch for inspecting the inside of the reaction tank.
As described later, when air is drawn into the treatment tank 30 by a fan or the like (not shown) through an air extraction pipe 38 provided in the treatment tank 30, the liquid containing dissolved oxygen permeates through the surface of the sponge carrier 23 in the housing 21 of the reaction tank 20, and supplies oxygen and the like to the sponge carrier 23 in the housing 21 of the reaction tank 20. Although sponge is taken up here as a suitable example of a carrier, it is not necessary to use a carrier 23 using sponge as the material for the porous body 24. For example, stone or hard resin generally used as a filter material for water treatment may be used instead of the carrier 23.

処理水槽30は、矩形の底板31と側壁32~35とからなる箱状体の本体30Aとからなり、前記前記反応槽20から排出された処理水や汚泥等の固形物を分離する。
前記処理水槽30には前記反応槽20から排出された処理水や汚泥等の固形物を集めて排出する水槽部36が設けられている。
また、前記処理水槽30には、浄化された処理水の他に処理水に含まれている固形物が排出されてくるので、底板31の傾斜は、前記処理水槽30に排出された処理水や固形物が自重により、底板31の上を滑り、側壁33から水槽部36方向に向かって送られていく傾斜角であることが必要である。しかしながら、底板31の傾斜角が大きいと処理水槽30の高さを大きくする必要に迫られることとなり、海上輸送用コンテナでは寸法規制の制限を受ける恐れが生じる。処理水槽30の高さの抑制を考慮すると底板31は、傾斜のない水平とすることが好ましいが、固定物が自重により堰37方向に向かって送られなくなってしまうので、固形物引き抜きを行う際には処理水槽30に溜まった処理水全量を固形物引き抜き管41の弁(図示せず)を開放して排出させたうえで、汚水を散水ろ床に散水させたまま、ろ床を通過して処理水槽30に滴下する処理水をシャワリングさせて底板31上にある溜った固形物を処理水とともに水平に近い緩い傾斜でも堰37方向に向かって送ることができるようになる。底板31に固形物がなくなったら、固形物引き抜き管41の弁を閉じて処理水槽30に処理水を貯留する。
これらを考慮すると傾斜角は、1/100~15/100が好ましく、5/100~10/100がより好ましい。
傾斜角が1/100を下回ると、処理水槽30に滴下する処理水によるシャワリングでは固定物が堰37方向に送られずに底板31上に堆積してしまいやすい。
また、傾斜角が15/100を上回ると、処理水槽30の高さが大きくなってしまい、海上輸送用コンテナの規制内の寸法に散水ろ床装置1を組み込むためには、散水ろ床の反応槽(20)の高さを低くする必要に迫られ、反応槽容量が小さくなってしまい、浄化能力を低下させてしまうことになる。海上輸送用コンテナの外寸法は、例えば10フィートタイプで長さ2,991mm×幅2,438mm×高さ2,591mmとなっており、高さ2,591mm内に抑える必要がある。12、20、40フィートタイプにおいても高さ2,591mmで規制されている。
The treated water tank 30 comprises a box-shaped main body 30A having a rectangular bottom plate 31 and side walls 32 to 35, and separates the treated water discharged from the reaction tank 20 and solids such as sludge.
The treated water tank 30 is provided with a water tank section 36 for collecting and discharging the treated water and solids such as sludge discharged from the reaction tank 20.
Moreover, since solid matter contained in the treated water is discharged into the treatment water tank 30 in addition to the purified treated water, the inclination of the bottom plate 31 must be such that the treated water and solid matter discharged into the treatment water tank 30 slide over the bottom plate 31 under their own weight and are sent from the side wall 33 toward the water tank section 36. However, if the inclination angle of the bottom plate 31 is large, it will be necessary to increase the height of the treatment water tank 30, which may result in restrictions on dimensions of containers for marine transport. Considering the need to keep the height of the treatment tank 30 down, it is preferable that the bottom plate 31 be horizontal and not inclined, but since the weight of the fixed objects would prevent them from being sent toward the weir 37, when removing the solids, the valve (not shown) of the solids removal pipe 41 is opened to discharge the entire amount of treated water accumulated in the treatment tank 30, and then, while the wastewater is being sprayed onto the trickling filter bed, the treated water that has passed through the filter bed and dripped into the treatment tank 30 is showered, so that the solids accumulated on the bottom plate 31 can be sent together with the treated water toward the weir 37 at a gentle incline close to horizontal. When there are no more solids on the bottom plate 31, the valve of the solids removal pipe 41 is closed and the treated water is stored in the treatment tank 30.
Considering these, the inclination angle is preferably 1/100 to 15/100, and more preferably 5/100 to 10/100.
If the inclination angle is less than 1/100, the solid objects are likely to accumulate on the bottom plate 31 instead of being sent toward the weir 37 by showering with the treated water dripping into the treated water tank 30 .
Furthermore, if the inclination angle exceeds 15/100, the height of the treatment tank 30 becomes large, and in order to incorporate the trickling filter device 1 within the dimensions regulated for marine transport containers, it is necessary to lower the height of the trickling filter reaction tank (20), which reduces the reaction tank capacity and reduces the purification capacity. For example, the external dimensions of a 10-foot marine transport container are 2,991 mm long x 2,438 mm wide x 2,591 mm high, and the height must be kept within 2,591 mm. The height is also regulated at 2,591 mm for 12-, 20-, and 40-foot types.

前記水槽部36には、処理水槽30に溜まった処理水を堰き止める堰37が設けられていて、通常の運転においては当該堰37の下を掻い潜った処理水が水槽部36に流れ、処理水引き抜き管40から排出する。
また、水槽部36には、処理水槽30内の空気を引き抜く空気引き抜き管38が設けられている。
当該空気引き抜き管38の先端38aは、水槽部36に貯留されている処理水の水面39より上となるように設けられている。
このように先端部38aの下が処理水で水封されているので、ファン(図示せず)等で空気を引き込むと反応槽20の上部から反応槽20を通過して空気引き抜き管38の中に空気が入り、それと同時に処理水槽30内の腐敗臭が排出される。
前記したように、当該空気引き抜き管38から空気を引き込むと、反応槽20の上部から空気引き抜き管38の中に空気が入って、それと同時に前記反応槽20の筐体21内のスポンジ担体23に対して空気等が供給される。
The water tank section 36 is provided with a dam 37 that holds back the treated water accumulated in the treatment water tank 30, and during normal operation, the treated water that slips under the dam 37 flows into the water tank section 36 and is discharged from the treated water withdrawal pipe 40.
In addition, the water tank section 36 is provided with an air extraction pipe 38 for extracting air from within the treatment water tank 30 .
The tip 38 a of the air extraction pipe 38 is provided so as to be above the water surface 39 of the treatment water stored in the water tank section 36 .
Since the area below tip 38a is sealed with treated water in this manner, when air is drawn in using a fan (not shown) or the like, the air passes through reaction tank 20 from the top and enters air extraction pipe 38, and at the same time, the putrid odor within treatment water tank 30 is expelled.
As described above, when air is drawn in through the air extraction pipe 38, air enters the air extraction pipe 38 from the top of the reaction tank 20, and at the same time, air etc. is supplied to the sponge carrier 23 inside the casing 21 of the reaction tank 20.

前記水槽部36には、当該水槽部36内に溜まった処理水や固形物を引く抜く固形物引き抜き管41が設けられている。
当該固形物引き抜き管41は、コンテナ型散水ろ床装置を稼働していくと底板31の傾斜部分に固形物が溜まるので、それを処理水と一緒に引き抜くためのものである。
このように構成された本件のコンテナ型散水ろ床装置1においては、散水ろ床装置の稼働において、底板31の傾斜部分に溜まった固形物を固形物引き抜き管41で処理水と一緒に引き抜き、前記処理水槽30内の処理水が空になった時に、反応槽20の上から処理水が滴下して散水され、雨のように降ってくるので、処理水を引き抜いた際に排出しきれなかった底板31上に堆積した固形物をきれいに洗浄できる。
このように本発明にかかるコンテナ型散水ろ床装置は、従来のように掻き寄せ機等の機械的な排出装置を設ける必要がないので、固形物を引き抜いたときに固形物の溜まりができず、処理水槽の中をきれいに掃除して中に溜まった固形物を排出できる。
The water tank section 36 is provided with a solid matter extraction pipe 41 for extracting the treated water and solid matter accumulated in the water tank section 36 .
The solids extraction pipe 41 is provided to extract solids that accumulate on the inclined portion of the bottom plate 31 during operation of the container-type trickling filter device together with the treated water.
In the container-type trickling bed device 1 of this invention configured as described above, during operation of the trickling bed device, solids accumulated on the inclined portion of the bottom plate 31 are extracted together with the treated water by the solids extraction pipe 41, and when the treated water in the treated water tank 30 becomes empty, the treated water is dripped and sprinkled from above the reaction tank 20, falling like rain, so that any solids accumulated on the bottom plate 31 that could not be completely discharged when the treated water was extracted can be thoroughly washed away.
As described above, the container-type trickling filter device of the present invention does not require the installation of a mechanical discharge device such as a scraper as in the conventional method, so that solids do not accumulate when they are pulled out, and the inside of the treatment tank can be cleaned thoroughly and the accumulated solids can be discharged.

本実施例におけるコンテナ型散水ろ床装置1においては、下部の処理水槽30において処理水や汚泥等の固形物を集めて排出する水槽部36を、コンテナ型散水ろ床装置1より水平方向の外側になるように構成している。これは反応槽内部を点検するための点検口27のスペースと装置上部のほうへ移動して点検作業に使用する梯子26のスペースを確保して十分に余裕をとった構造としているためである。他の実施例として、図8に示すように反応槽容量を大きくして、反応槽内部を点検するための点検口27や点検作業用の梯子26を海上輸送用コンテナの寸法規制の範囲内に収めた構造としたうえで、コンテナ型散水ろ床の性能を最大限に高めるために前記水槽部36をコンテナ型散水ろ床装置1より水平方向の内側になるように構成しても良い。 In the container-type trickling filter device 1 in this embodiment, the water tank section 36 that collects and discharges treated water and solids such as sludge in the lower treated water tank 30 is configured to be horizontally outside the container-type trickling filter device 1. This is because the structure has sufficient space to secure the space for the inspection hatch 27 for inspecting the inside of the reaction tank and the ladder 26 that is moved toward the top of the device and used for inspection work. As another embodiment, as shown in Figure 8, the reaction tank capacity may be increased, and the inspection hatch 27 for inspecting the inside of the reaction tank and the ladder 26 for inspection work may be configured to fit within the dimensional regulations of marine transport containers, and the water tank section 36 may be configured to be horizontally inside the container-type trickling filter device 1 to maximize the performance of the container-type trickling filter.

図6においては、汚水中の窒素除去のために処理水をコンテナ型散水ろ床装置1の汚水供給側の配管に図示しないポンプで循環させる循環用処理水引き抜き管42を設けた実施例を示す。汚水中のアンモニアを好気性の反応槽20で硝化反応させ、硝酸性窒素を含む処理水を反応槽20に循環させて、反応槽20に介在する通性嫌気性細菌である脱窒細菌の作用で脱窒反応させて窒素除去を行う。処理水引き抜き管40と循環用処理水引き抜き管42は越流トラフ43とつながっており、越流トラフ43の処理水引き抜き管40と循環用処理水引き抜き管42の間には隔て板44が移動可能に設けられる。隔て板44は循環用処理水の循環量を決定するために、設置位置を図中の矢印の方向に調整可能にしている。即ち、窒素除去率を高めるべきときには隔て板44を処理水引き抜き管40側に近づけて処理水の循環量を多くする。反対に窒素除去率を高める必要のないときには隔て板44を循環用処理水引き抜き管42側に近づけて処理水の循環量を少なくする。 In FIG. 6, an embodiment is shown in which a treated water withdrawal pipe for circulation 42 is provided to circulate treated water to the piping on the wastewater supply side of the container-type trickling filter device 1 by a pump (not shown) in order to remove nitrogen from the wastewater. Ammonia in the wastewater is nitrified in the aerobic reaction tank 20, and treated water containing nitrate nitrogen is circulated to the reaction tank 20, where nitrogen is removed by denitrification reaction caused by the action of denitrifying bacteria, which are facultative anaerobic bacteria present in the reaction tank 20. The treated water withdrawal pipe 40 and the treated water withdrawal pipe for circulation 42 are connected to the overflow trough 43, and a partition plate 44 is movably installed between the treated water withdrawal pipe 40 and the treated water withdrawal pipe for circulation 42 of the overflow trough 43. The installation position of the partition plate 44 can be adjusted in the direction of the arrow in the figure in order to determine the amount of treated water to be circulated for circulation. That is, when the nitrogen removal rate needs to be increased, the partition plate 44 is moved closer to the treated water withdrawal pipe 40 side to increase the amount of treated water to be circulated. Conversely, when there is no need to increase the nitrogen removal rate, the partition plate 44 is moved closer to the circulating treated water withdrawal pipe 42 to reduce the amount of circulating treated water.

図9は、本発明のコンテナ型散水ろ床装置1の他の実施例を表す図で、空気引き抜き管38内が湿潤して結露すると水溜まりが生じるので、図示していないファン等の機器で吸引するとファンが水を吸込んで損傷してしまう恐れがある。そこで、当該空気引き抜き管38の途中にドレン管45を設け、空気引き抜き管38内の水溜まりを処理水引き抜き管40へ排出するようにしている。排出先は処理水引き抜き管40に限らず、固形物引き抜き管41でもよいし、ドレン管45を水槽部36の側壁32に穴あけ加工を施して接続してもよい。 Figure 9 shows another embodiment of the container-type trickling filter device 1 of the present invention. When the inside of the air extraction pipe 38 becomes wet and condenses, water pools form, and if a fan or other device (not shown) is used to suck in the water, the fan may be damaged. Therefore, a drain pipe 45 is provided midway through the air extraction pipe 38, and the water pool in the air extraction pipe 38 is discharged to the treated water extraction pipe 40. The discharge destination is not limited to the treated water extraction pipe 40, but may be the solids extraction pipe 41, or the drain pipe 45 may be connected to the side wall 32 of the water tank section 36 by drilling a hole in the pipe.

図10は、本発明のコンテナ型散水ろ床装置1の他の実施例を表す図で、空気引き抜き管38を、当該空気引き抜き管38の先端38aが下となるように傾斜をつけている例を示している。これにより空気引き抜き管38内に発生した露水は処理水槽30内に排出されて、空気引き抜き管38内の水溜まりを避けることができる。 Figure 10 shows another embodiment of the container-type trickling filter device 1 of the present invention, in which the air extraction pipe 38 is inclined so that the tip 38a of the air extraction pipe 38 is downward. This allows dew water generated in the air extraction pipe 38 to be discharged into the treated water tank 30, preventing water from pooling in the air extraction pipe 38.

図11から図13は、本発明のコンテナ型散水ろ床装置の他の実施例を表す図である。
図11は、前記反応槽20の構成を表す図である。
図12においては、図1に示されたコンテナ型散水ろ床装置1の処理水槽30をコンクリート等の土木躯体とした実施例を示している。この例では、海上輸送用コンテナの寸法規制内で、図1で処理水槽30が占めていたスペースを、コンテナ型散水ろ床装置1の反応槽20の容量に置き換えて増やすことができる。また、シャワリングにより緩い傾斜の底板31上の堆積物を排出することが可能なので、コンテナ型散水ろ床装置1の高さを低くでき、コンパクト化のメリットがある。従って、コンテナ型散水ろ床装置1の容量増加によって浄化能力を向上させつつも、コンテナ型散水ろ床装置1の高さ方向のスペースを抑えることができる。
11 to 13 are diagrams showing another embodiment of the container-type trickling filter device of the present invention.
FIG. 11 is a diagram showing the configuration of the reaction tank 20.
In Fig. 12, an embodiment is shown in which the treated water tank 30 of the container-type trickling filter device 1 shown in Fig. 1 is made of a civil engineering structure such as concrete. In this example, the space occupied by the treated water tank 30 in Fig. 1 can be replaced with the capacity of the reaction tank 20 of the container-type trickling filter device 1 within the dimensional regulations of marine transport containers, and can be increased. In addition, since it is possible to discharge the deposits on the gently sloping bottom plate 31 by showering, the height of the container-type trickling filter device 1 can be reduced, which has the advantage of making it compact. Therefore, while improving the purification capacity by increasing the capacity of the container-type trickling filter device 1, the space in the height direction of the container-type trickling filter device 1 can be reduced.

図13においては、図12と同様に処理水槽30を土木躯体とした実施例であり反応槽20を2段積みとしている。 In Figure 13, as in Figure 12, the treatment tank 30 is an example in which a civil engineering structure is used, and the reaction tanks 20 are stacked in two layers.

図12及び13に示すように反応槽20を複数個の筐体21で構成し、横方向に増やしたり上下方向に筐体21の個数を変えたりすることでコンテナ型散水ろ床装置1の高さや、容積を変更することができる。 As shown in Figures 12 and 13, the reaction tank 20 is composed of multiple housings 21, and the height and volume of the container-type trickling filter device 1 can be changed by increasing the number of housings 21 horizontally or changing the number of housings 21 vertically.

本発明の実施例においては、コンテナ型散水ろ床装置の外枠(51~54)に海上輸送用コンテナを利用しているが、これに限定されるものではなく本発明の特徴はコンテナ型散水ろ床装置における下部の処理水槽の構造にある。 In the embodiment of the present invention, a marine transport container is used for the outer frame (51-54) of the container-type trickling filter device, but this is not limited to this, and the feature of the present invention is the structure of the treated water tank at the bottom of the container-type trickling filter device.

1:コンテナ型散水ろ床装置
20:反応槽
21:筐体
22:底板
23:スポンジ担体
26:梯子
27:点検口
30:処理水槽
31A:本体
31:底板
32~35:側壁
36:水槽部
37:堰
38:空気引き抜き管
40:処理水引き抜き管
41:固形物引き抜き管
42:循環用処理水引き抜き管
43:越流トラフ
44:隔て板
45:ドレン管
50:土木躯体
1: Container-type trickling filter device 20: Reaction tank 21: Housing 22: Bottom plate 23: Sponge carrier 26: Ladder 27: Inspection hatch 30: Treated water tank 31A: Main body 31: Bottom plate 32-35: Side wall 36: Water tank section 37: Weir 38: Air extraction pipe 40: Treated water extraction pipe 41: Solids extraction pipe 42: Circulating treated water extraction pipe 43: Overflow trough 44: Partition plate 45: Drain pipe 50: Civil engineering structure

Claims (8)

反応槽(20)と反応槽(20)の内部を点検する点検口(27)と処理水槽(30)とからなる散水ろ床装置(1)であって、前記反応槽(20)は、気密性を備えた直方体からなる筐体(21)と、該筐体(21)の底部設けられたメッシュ状の底板(22)と、前記該筐体(21)内に充填された担体(23)とからなり、前記処理水槽(30)は、処理水の排出方向に向かって少なくとも1/100~15/100の勾配を設けている傾斜した長方形の底板(31)と、側壁(32~35)とからなる箱状体の本体(30A)と、
当該本体(30A)の処理水排出方向に設けられた水槽部(36)と、当該水槽部(36)に設けられた堰(37)と、空気引き抜き管(38)と、処理水引き抜き管(40)と、固形物引き抜き管(41)からなり、かつ前記水槽部(36)は散水ろ床装置(1)より水平方向の外側になるように構成されている
ことを特徴とするコンテナ型散水ろ床装置。
A trickling filter device (1) comprising a reaction tank (20), an inspection hatch (27) for inspecting the inside of the reaction tank (20) , and a treated water tank (30), wherein the reaction tank (20) comprises an airtight rectangular parallelepiped housing (21), a mesh-like bottom plate (22) provided at the bottom of the housing (21), and a carrier (23) filled in the housing (21), and the treated water tank (30) comprises a box-shaped main body (30A) comprising an inclined rectangular bottom plate (31) having a gradient of at least 1/100 to 15/100 toward the discharge direction of the treated water, and side walls (32 to 35);
The system comprises a water tank section (36) provided in the treated water discharge direction of the main body (30A), a weir (37) provided in the water tank section (36), an air withdrawal pipe (38), a treated water withdrawal pipe (40), and a solid matter withdrawal pipe (41), and the water tank section (36) is configured to be horizontally outward of the trickling filter bed device (1).
A container-type trickling filter device characterized by the above.
前記水槽部(36)に循環用処理水引き抜き管(42)を設けたことを特徴とする請求項1記載のコンテナ型散水ろ床装置。 The container-type trickling filter device according to claim 1, characterized in that a circulating treated water withdrawal pipe (42) is provided in the water tank section (36). 前記処理水槽(30)内に越流トラフ(43)を設け、当該越流トラフ(43)につながっている処理水引き抜き管(40)と循環用処理水引き抜き管(42)の間に隔て板(44)を移動可能に設けたこと特徴とする請求項2に記載のコンテナ型散水ろ床装置。 The container-type trickling filter device according to claim 2, characterized in that an overflow trough (43) is provided in the treated water tank (30), and a partition plate (44) is movably provided between the treated water withdrawal pipe (40) connected to the overflow trough (43) and the circulating treated water withdrawal pipe (42). 前記空気引き抜き管(38)の途中に、該空気引き抜き管(38)内から水溜まりを排出するドレン管(45)を設けたことを特徴とする請求項1から3の何れか1に記載のコンテナ型散水ろ床装置。 A container-type trickling filter device according to any one of claims 1 to 3, characterized in that a drain pipe (45) for discharging water from within the air extraction pipe (38) is provided midway along the air extraction pipe (38). 前記空気引き抜き管(38)を当該空気引き抜き管(38)の先端(38a)が下となるように傾斜をつけていることを特徴とする請求項1から4の何れか1に記載のコンテナ型散水ろ床装置。 A container-type trickling filter device according to any one of claims 1 to 4, characterized in that the air extraction pipe (38) is inclined so that the tip (38a) of the air extraction pipe (38) is downward. 前記散水ろ床装置(1)の前記処理水槽(30)を土木躯体とし、海上輸送用コンテナの寸法規制内で、前記処理水槽(30)が占めていたスペースを、前記散水ろ床装置(1)の前記反応槽(20)の容量に置き換えて増やすことを特徴とする請求項1からの何れか1に記載のコンテナ型散水ろ床装置。 A container-type trickling filter device as described in any one of claims 1 to 5, characterized in that the treated water tank (30) of the trickling filter device (1) is made into a civil engineering structure, and the space occupied by the treated water tank (30) is replaced and increased by the capacity of the reaction tank (20 ) of the trickling filter device (1) within the dimensional regulations of marine transport containers. 前記反応槽(20)を複数段の前記筐体(21)で構成し、当該筐体(21)の個数を変えることで前記散水ろ床装置(1)の高さや、容積を変更することを特徴とする請求項に記載のコンテナ型散水ろ床装置。 The container-type trickling bed device according to claim 6, characterized in that the reaction tank (20) is composed of a plurality of stages of the housings (21), and the height and volume of the trickling bed device (1) are changed by changing the number of the housings ( 21 ). 固形物引き抜きを行う際には処理水槽(30)に溜まった処理水全量を固形物引き抜き管(41)の弁を開放して排出させたうえで、汚水を散水ろ床に散水させたまま、ろ床を通過して処理水槽(30)に滴下する処理水をシャワリングさせて底板(31)上にある溜った固形物を処理水とともに水平に近い緩い傾斜でも堰(37)方向に向かって送ることを特徴とする請求項1からの何れか1に記載のコンテナ型散水ろ床装置の処理水槽(30)の洗浄方法。 A method for cleaning the treated water tank (30) of a container-type trickling filter apparatus as described in any one of claims 1 to 7, characterized in that when removing solids, the valve of the solids removal pipe (41) is opened to discharge the entire amount of treated water accumulated in the treated water tank (30), and then, while the wastewater is being sprayed onto the trickling filter bed, the treated water that passes through the filter bed and drips into the treated water tank (30) is showered to send the accumulated solids on the bottom plate (31) together with the treated water toward the weir ( 37 ) even at a gentle incline close to horizontal.
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US20180134594A1 (en) 2010-09-07 2018-05-17 Liberty Evans, Llc Wastewater treatment system design
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US20180134594A1 (en) 2010-09-07 2018-05-17 Liberty Evans, Llc Wastewater treatment system design
JP2014004522A (en) 2012-06-25 2014-01-16 Tottori Prefecture Deodorization apparatus for livestock excrement, livestock farming by-products and the like
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