JP6652898B2 - Water treatment device and water treatment method - Google Patents

Water treatment device and water treatment method Download PDF

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JP6652898B2
JP6652898B2 JP2016162841A JP2016162841A JP6652898B2 JP 6652898 B2 JP6652898 B2 JP 6652898B2 JP 2016162841 A JP2016162841 A JP 2016162841A JP 2016162841 A JP2016162841 A JP 2016162841A JP 6652898 B2 JP6652898 B2 JP 6652898B2
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惇太 高橋
惇太 高橋
米山 豊
豊 米山
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Swing Corp
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    • 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
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    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

本発明は、水処理装置及び水処理方法に関し、特に、下水や食品工場などから排出される有機性排水を散水ろ床式水処理装置を用いて処理する水処理装置及び水処理方法に関する。   The present invention relates to a water treatment apparatus and a water treatment method, and more particularly, to a water treatment apparatus and a water treatment method for treating organic wastewater discharged from sewage and food factories using a trickling filter type water treatment apparatus.

散水ろ床型の水処理技術は、標準活性汚泥法に比べ、曝気が不要であることから、消費電力が少ない、汚泥発生量が少なく余剰汚泥の処分コストを削減できるといった特徴をもつ。そのため、近年、電気などのインフラが整備されていない東南アジア等の発展途上国における下水処理などへの適用が検討されている。   The trickling filter type water treatment technology has the characteristics that it does not require aeration as compared with the standard activated sludge method, so that it consumes less power, generates less sludge, and can reduce the disposal cost of excess sludge. Therefore, in recent years, application to sewage treatment and the like in developing countries such as Southeast Asia where infrastructure such as electricity has not been developed has been studied.

一方で、散水ろ床型の水処理技術は、散水ろ床のろ材上に汚泥が付着するため、付着した汚泥が腐敗することにより悪臭が発生し、またはこの汚泥に起因して、ろ床バエとよばれるチョウバエの一種が発生することが知られている。このような悪臭及びろ床バエの発生により、維持管理を行う際の作業環境が悪化するという問題がある。   On the other hand, in the water treatment technology of the trickling filter type, since sludge adheres to the filter medium of the trickling filter bed, the attached sludge rots, resulting in a bad smell. It is known that a kind of Drosophila, called soybean, occurs. There is a problem that the working environment when performing maintenance is deteriorated due to the generation of such bad smells and filter flies.

悪臭及びろ床バエの発生を抑制するために、例えば、特許文献1(特開昭58−34088号公報)は、アルカリ性溶液を散水ろ床に接触させて、散水ろ床内を洗浄する方法が記載されている。   For example, Patent Document 1 (Japanese Patent Application Laid-Open No. 58-34088) discloses a method of contacting an alkaline solution with a trickling filter to wash the inside of the trickling filter in order to suppress the generation of offensive odor and filter flies. Has been described.

特許文献2(国際公開第12/161339号)は、固液分離装置と散水ろ床とを備えた下水処理システムにおいて、散水ろ床内のろ材充填層を洗浄する洗浄手段を設ける技術が記載されている。   Patent Literature 2 (International Publication No. 12/161339) describes a technique in which a sewage treatment system including a solid-liquid separation device and a sprinkling filter bed is provided with a washing means for washing a filter medium packed layer in the sprinkling filter bed. ing.

特許文献3(特開2015−33666号公報)は、洗浄手段を備えた散水ろ床と生物処理槽とを備え、生物処理槽内において昇温された空気で散水ろ床を暖めることにより散水ろ床を加温する技術が記載されている。非特許文献1は、散水ろ床型硝化脱窒反応器において、散水ろ床部を定期洗浄することが記載されている。   Patent Literature 3 (Japanese Patent Application Laid-Open No. 2015-33666) includes a water trickling filter provided with a washing means and a biological treatment tank, and the water trickling filter is heated by warming the water trickling bed in the biological treatment tank. Techniques for heating the floor are described. Non-Patent Document 1 describes that a sprinkling filter section is periodically cleaned in a sprinkling filter type nitrification and denitrification reactor.

特開昭58−34088号公報JP-A-58-34088 国際公開第12/161339号International Publication No. 12/161339 特開2015−33666号公報JP 2015-33666 A

「ろ床洗浄による散水ろ床法のPsychodidae発生抑制効果」、2016年水環境学会年会講演集、p68“Effects of Psychodidae Generation Suppression by Sprinkling Filter Method by Filter Filter Cleaning”, Proceedings of Annual Meeting of Japan Society on Water Environment 2016, p68

しかしながら、特許文献1の技術では、薬品添加により薬液コストがかかるうえ、薬品添加により装置内のろ床を劣化させる恐れがある。特許文献2〜3及び非特許文献の技術は、いずれも散水ろ床を冠水することで散水ろ床を洗浄しているが、散水ろ床の洗浄時には散水ろ床に接続された他の水処理装置の運転を一部停止させる必要があり、作業効率が低下する。更に、特許文献2及び3及び非特許文献1の技術では、散水ろ床を冠水させて洗浄することにより高濁度の洗浄排水が発生し、この洗浄排水を別途、浄化しなければならないという問題もある。   However, in the technique of Patent Literature 1, a chemical solution is costly due to the addition of a chemical, and the filter bed in the apparatus may be deteriorated by the addition of the chemical. The techniques of Patent Documents 2 and 3 and Non-Patent Documents all wash the trickling filter bed by flooding the trickling filter bed, but other water treatment connected to the trickling filter bed at the time of washing the trickling filter bed. It is necessary to partially stop the operation of the device, and the work efficiency is reduced. Furthermore, in the techniques of Patent Literatures 2 and 3 and Non-Patent Literature 1, a high turbidity cleaning wastewater is generated by submerging and washing the trickling filter bed, and this cleaning wastewater must be separately purified. There is also.

本発明は、上記課題に鑑みてなされたものであり、水処理装置の運転を停止させることなく、効率良く悪臭及びろ床バエの発生を抑制可能な水処理装置及び水処理方法を提供する。   The present invention has been made in view of the above problems, and provides a water treatment apparatus and a water treatment method that can efficiently suppress the generation of offensive odor and filter bed flies without stopping the operation of the water treatment apparatus.

上記目的を達成するために本発明者らが鋭意検討したところ、散水ろ床式装置と浸漬ろ床式装置の機能を両立する反応槽を少なくとも2槽連結し、これらに供給する原水の流路を所定のタイミングで切り替えることが有効であることを見いだした。   In order to achieve the above object, the present inventors have conducted intensive studies. As a result, at least two reaction tanks having both functions of a sprinkling filter type apparatus and a submerged filter type apparatus are connected, and a flow path of raw water supplied to these is connected. It is found that it is effective to switch at a predetermined timing.

以上の知見を基礎として完成した本発明は一側面において、微生物を付着した第1の担体層を備える第1槽と、第1槽の後段に接続され、微生物を付着した第2の担体層を備える第2槽と、第1槽又は第2槽へ原水を供給可能な原水供給路と、原水の供給を、第1槽と第2槽との間で切り替える切替手段とを備え、切替手段が原水の供給を第1槽に切り替えることにより、第1槽が原水中に第1の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理し、第2槽が第1槽で得られた処理水を第2の担体層の上部から散布して生物処理する散水ろ床法により処理水を処理し、切替手段が原水の供給を第2槽に切り替えることにより、第2槽が原水中に第2の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理し、第1槽が第2槽で得られた処理水を第1の担体層の上部から散布して生物処理する散水ろ床法により処理水を処理する水処理装置が提供される。   In one aspect, the present invention, which has been completed on the basis of the above findings, includes a first tank provided with a first carrier layer to which microorganisms are attached, and a second carrier layer connected to a subsequent stage of the first tank and to which microorganisms are attached. A second tank provided, a raw water supply path capable of supplying raw water to the first tank or the second tank, and switching means for switching the supply of raw water between the first tank and the second tank. By switching the supply of raw water to the first tank, the first tank treats the raw water by the immersion filter method in which the first carrier layer is immersed in the raw water and biologically treated, and the second tank is obtained in the first tank. The treated water is treated by a sprinkling filter method in which the treated water is sprayed from above the second carrier layer to biologically treat the treated water, and the switching means switches the supply of the raw water to the second tank. Raw water is treated by the immersion filter method in which the second carrier layer is immersed in water and biologically treated, and the first tank is the second tank Water treatment apparatus the treated water obtained by dispersing from the top of the first carrier layer processing the treated water by trickling filter method of biological treatment is provided.

本発明に係る水処理装置は一実施態様において、散水ろ床法により処理される側の槽の汚染具合に基づいて切替手段による切替操作を制御する制御手段を備える。   In one embodiment, the water treatment apparatus according to the present invention includes control means for controlling the switching operation by the switching means based on the degree of contamination of the tank to be treated by the trickling filter method.

本発明に係る水処理装置は別の一実施態様において、第1槽及び第2槽の処理水出口に配置されたスクリーンを備え、制御手段が、スクリーンに捕捉された固形物量に基づいて、散水ろ床法により処理される側の槽の汚染具合を判断することを含む。   In another embodiment, the water treatment apparatus according to the present invention includes a screen disposed at a treated water outlet of the first tank and the second tank, and the control unit sprays water based on an amount of solids captured on the screen. This includes determining the degree of contamination of the tank to be treated by the filter bed method.

本発明に係る水処理装置は更に別の一実施態様において、第1の担体層又は第2の担体層に付着する担体付着生物量に基づいて、制御手段が、散水ろ床法により処理される側の槽の汚染具合を判断することを含む。   In still another embodiment of the water treatment apparatus according to the present invention, the control means is treated by a trickling filter method on the basis of the amount of biomass attached to the first carrier layer or the second carrier layer. Determining the degree of contamination of the side tank.

本発明は別の一側面において、微生物を付着した第1の担体層を原水に浸漬して生物処理する浸漬ろ床槽と、微生物を付着した第2の担体層を備え、浸漬ろ床槽からの処理水を、第2の担体層の上部から散布して接触させることにより生物処理する散水ろ床槽と、原水を浸漬ろ床槽又は散水ろ床槽へ供給するための原水供給路と、原水の供給を浸漬ろ床槽側又は散水ろ床槽側へと切り替える切替手段とを備え、切替手段が、原水の供給を浸漬ろ床槽側から散水ろ床槽側へと切り替えることにより、散水ろ床槽内に原水を流入させて散水ろ床槽内を原水で満たして散水ろ床槽を洗浄するとともに、散水ろ床槽の洗浄水を浸漬ろ床槽側へ供給して生物処理することを特徴とする水処理装置が提供される。   According to another aspect of the present invention, there is provided an immersion filter tank for immersing a first carrier layer to which microorganisms are attached in raw water for biological treatment, and a second carrier layer having microorganisms attached thereto. Treated water is sprayed from the upper part of the second carrier layer and sprayed and contacted by biological treatment, and a raw water supply path for supplying raw water to the immersion filter tank or the water filter bed tank, Switching means for switching the supply of raw water to the immersion filter tank side or the sprinkling filter tank side, and the switching means switches the supply of the raw water from the immersion filter tank side to the sprinkling filter tank side to thereby sprinkle water. Inject raw water into the filter bed tank, fill the inside of the sprinkler filter tank with raw water to wash the sprinkler filter tank, and supply the washing water of the sprinkler filter tank to the immersion filter tank side for biological treatment. A water treatment apparatus is provided.

本発明は別の一側面において、微生物を付着した第1の担体層を備える第1槽に原水を供給し、第1槽において原水中に第1の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理するとともに、第1槽の後段に接続され、微生物を付着した第2の担体層を備える第2槽において、第1槽で得られた処理水を第2の担体層の上部から散布して生物処理する散水ろ床法により処理水を処理することと、原水を第1槽から第2槽へ供給するように切り替えることと、第2槽において原水中に第2の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理するとともに、第1槽において、第2槽で得られた処理水を第1の担体層の上部から散布して生物処理する散水ろ床法により処理することを含む水処理方法が提供される。   In another aspect of the present invention, raw water is supplied to a first tank provided with a first carrier layer to which microorganisms are attached, and the first carrier layer is immersed in the raw water in the first tank to perform biological treatment. In the second tank provided with the second carrier layer attached to the microorganisms and connected to the subsequent stage of the first tank while treating the raw water by the bed method, the treated water obtained in the first tank is used as the second carrier layer. Treating the treated water by a sprinkling filter method of spraying from the upper part and biologically treating, switching the raw water to be supplied from the first tank to the second tank, and providing the second carrier in the raw water in the second tank. Raw water is treated by the immersion filter bed method in which the layer is immersed for biological treatment, and in the first tank, the treated water obtained in the second tank is sprayed from the upper part of the first carrier layer to perform biological treatment. A water treatment method is provided that includes treating by a bed method.

本発明によれば、水処理装置の運転を停止させることなく、効率良く悪臭及びろ床バエの発生を抑制可能な水処理装置及び水処理方法が提供できる。   ADVANTAGE OF THE INVENTION According to this invention, the water treatment apparatus and water treatment method which can suppress generation | occurrence | production of a bad smell and a filter bed fly efficiently without stopping operation | movement of a water treatment apparatus can be provided.

本発明の実施の形態に係る水処理装置の一例を示す概略図である。It is a schematic diagram showing an example of a water treatment device concerning an embodiment of the invention. 図1に示す水処理装置において、第1槽に浸漬ろ床法による処理を適用し、第2槽に散水ろ床法による処理を適用した場合の水処理の例を表す概略図である。FIG. 2 is a schematic diagram illustrating an example of water treatment in a case where a treatment by a dipping filter method is applied to a first tank and a treatment by a sprinkling filter method is applied to a second tank in the water treatment apparatus shown in FIG. 1. 図1に示す水処理装置において、第1槽に散水ろ床法による処理を適用し、第2槽に浸漬ろ床法による処理を適用した場合の水処理の例を表す概略図である。FIG. 2 is a schematic diagram illustrating an example of water treatment in a case where a treatment by a trickling filter method is applied to a first tank and a treatment by a dipping filter method is applied to a second tank in the water treatment apparatus shown in FIG. 1. 図1に示す水処理装置の変形例に係る水処理装置の一例を示す概略図である。It is the schematic which shows an example of the water treatment apparatus which concerns on the modification of the water treatment apparatus shown in FIG. 本発明の実施の形態の変形例に係る水処理装置の一例を示す概略図であり、第1槽及び第3槽に浸漬ろ床法による処理を適用し、第2槽及び第4槽に散水ろ床法による処理を適用した場合の水処理の例を表す概略図である。It is the schematic which shows an example of the water treatment apparatus which concerns on the modification of embodiment of this invention, applying the process by the immersion filter method to a 1st tank and a 3rd tank, and watering a 2nd tank and a 4th tank. It is a schematic diagram showing the example of the water treatment at the time of applying the treatment by the filter bed method. 本発明の実施の形態の変形例に係る水処理装置の一例を示す概略図であり、第1槽及び第3槽に散水ろ床法による処理を適用し、第2槽及び第4槽に浸漬ろ床法による処理を適用した場合の水処理の例を表す概略図である。It is the schematic which shows an example of the water treatment apparatus which concerns on the modification of embodiment of this invention, applying the process by the trickling filter method to a 1st tank and a 3rd tank, and immersing in a 2nd tank and a 4th tank. It is a schematic diagram showing the example of the water treatment at the time of applying the treatment by the filter bed method. 本発明の実施の形態の別の変形例に係る水処理装置の一例を示す概略図であり、第1槽に散水ろ床法、第2槽に上向流の浸漬ろ床法を適用した場合を表す概略図である。It is the schematic which shows an example of the water treatment apparatus which concerns on another modification of embodiment of this invention, and applies the sprinkling filter method to a 1st tank, and the immersion filter method of an upward flow to a 2nd tank. FIG. 本発明の実施の形態の別の変形例に係る水処理装置の一例を示す概略図であり、第1槽に上向流の浸漬ろ床法、第2槽に散水ろ床法を適用した場合を表す概略図である。It is the schematic which shows an example of the water treatment apparatus which concerns on another modification of embodiment of this invention, When the upflow immersion filter method is applied to a 1st tank, and the sprinkling filter method is applied to a 2nd tank. FIG. 本発明の実施の形態に係る水処理装置を組み込んだ水処理システムの例を表す概略図である。1 is a schematic diagram illustrating an example of a water treatment system incorporating a water treatment device according to an embodiment of the present invention. 本発明の実施の形態に係る水処理装置を既存の水処理設備に組み込んだ場合の水処理システムの例を表す概略図である。It is a schematic diagram showing the example of the water treatment system at the time of incorporating the water treatment device concerning an embodiment of the invention into existing water treatment equipment. 実施例及び比較例に係る水処理装置の装置立ち上げ時のBOD容積負荷の推移と経過日数との関係を表すグラフである。It is a graph showing the relationship between transition of BOD volume load at the time of device start-up of the water treatment device according to the example and the comparative example and the elapsed days.

以下、図面を参照しながら本発明の実施の形態を説明する。以下に示す実施の形態は、この発明の技術的思想を具体化するための装置や方法を例示するものであってこの発明の技術的思想は構成部品の構造、配置等を下記のものに特定するものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. The embodiments described below exemplify an apparatus and a method for embodying the technical idea of the present invention. The technical idea of the present invention specifies the structure, arrangement, and the like of the components as follows. It does not do.

図1に示すように、本発明の実施の形態に係る水処理装置は、微生物を付着した第1の担体層31を備える第1槽3と微生物を付着した第2の担体層41を備える第2槽4と、第1槽3又は第2槽4へ原水を供給可能な原水供給路12a、12bと、原水の供給を、第1槽3と第2槽4との間で切り替える切替手段5とを備える。   As shown in FIG. 1, the water treatment apparatus according to the embodiment of the present invention includes a first tank 3 having a first carrier layer 31 having microorganisms attached thereto and a second tank having a second carrier layer 41 having microorganisms attached thereto. Switching means 5 for switching between the two tanks 4, the raw water supply paths 12a and 12b capable of supplying raw water to the first tank 3 or the second tank 4, and the supply of raw water between the first tank 3 and the second tank 4. And

第1槽3の前段には、原水を貯蔵するための原水槽1が配置されている。第1槽3の後段には、第2槽4が配管13を介して接続されている。第2槽4の後段には、配管14を介して第2槽4の処理液を貯蔵するための処理水槽7が配置されている。   A raw water tank 1 for storing raw water is disposed in front of the first tank 3. A second tank 4 is connected to the subsequent stage of the first tank 3 via a pipe 13. A processing water tank 7 for storing the processing liquid in the second tank 4 via a pipe 14 is disposed downstream of the second tank 4.

第1槽3及び第2槽4としては、散水ろ床式装置と浸漬ろ床式装置の機能を両立する反応槽であればよい。具体的には、第1槽3及び第2槽4は、内部に担体を充填することにより形成されるろ床を有し、処理対象となる流体(処理流体)をろ床の上方から散布可能で、且つろ床を一定期間冠水させることが可能な形式の反応槽であれば特に限定されない。第1槽3及び第2槽4は、互いに同一形状であっても異なる形状であってもよい。   The first tank 3 and the second tank 4 may be reaction tanks that have both the functions of the trickling filter apparatus and the immersion filter apparatus. Specifically, the first tank 3 and the second tank 4 each have a filter bed formed by filling a carrier therein, and can spray a fluid to be treated (treatment fluid) from above the filter bed. The reaction tank is not particularly limited as long as it is a type of reaction tank capable of flooding the filter bed for a certain period. The first tank 3 and the second tank 4 may have the same shape or different shapes.

第1の担体層31及び第2の担体層41を構成する担体の素材としては、微生物が付着すればどのような素材でもよく、例えば、プラスチック、砕石などが好適に用いられる。担体の形状は、プレート状、球状、楕円球体状、柱状、直方体状、中空状、筒状などのいずれの形状であってもよい。   As a material of the carrier constituting the first carrier layer 31 and the second carrier layer 41, any material may be used as long as microorganisms adhere thereto. For example, plastic, crushed stone and the like are suitably used. The shape of the carrier may be any shape such as a plate, a sphere, an ellipsoidal sphere, a column, a rectangular parallelepiped, a hollow, and a tube.

第1槽3及び第2槽4の上方から第1の担体層31及び第2の担体層41へ処理流体を散水する具体的構成も特に限定されない。即ち、散水にあたっては、ろ床全体に処理流体が散水されるような態様であればよく、多孔板、スプリンクラー型又はスパイラル型のノズル、自走式の回転散水機等のいずれの方式でもよい。第1槽3と第2槽4とを繋ぐ配管13としては、例えば、サイフォン等を採用することにより、第1槽3と第2槽4との間を流れる処理流体を少ない動力で流すことができる。   The specific configuration for spraying the processing fluid onto the first carrier layer 31 and the second carrier layer 41 from above the first tank 3 and the second tank 4 is not particularly limited. That is, watering may be performed in any form as long as the treatment fluid is sprayed on the entire filter bed, and may be any of a perforated plate, a sprinkler type or a spiral type nozzle, and a self-propelled rotary watering machine. As the pipe 13 connecting the first tank 3 and the second tank 4, for example, a siphon or the like is employed so that the processing fluid flowing between the first tank 3 and the second tank 4 can flow with little power. it can.

第1槽3及び第2槽4は、一方の槽が「散水ろ床槽」として機能する場合には、他方の槽が「浸水ろ床槽」として機能する。即ち、図2に示すように、原水の供給が、ポンプ11及び切替手段5及び原水供給路12aを介して第1槽3に行われる場合には、第1槽3が、原水中に第1の担体層31を浸漬して生物処理する浸漬ろ床法により原水を処理する「浸漬ろ床槽」として機能し、第2槽4が、第1槽3で得られた処理水を第2の担体層41の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能する。   When one of the first and second tanks 3 and 4 functions as a “watering filter tank”, the other tank functions as a “flooding filter tank”. That is, as shown in FIG. 2, when the raw water is supplied to the first tank 3 via the pump 11, the switching means 5, and the raw water supply path 12a, the first tank 3 Function as a "immersion filter tank" for treating raw water by the immersion filter method in which the carrier layer 31 is immersed and biologically treated, and the second tank 4 uses the treated water obtained in the first tank 3 for the second treatment. It functions as a "watering filter tank" which treats treated water by the watering filter method of spraying from the upper part of the carrier layer 41 and biologically treating it.

図2において、第2槽4から流出する処理水の一部は、ポンプ17により引き抜かれて、配管14、15a、15b及び15cを通って配管13から第2槽4に循環させてもよい。   In FIG. 2, part of the treated water flowing out of the second tank 4 may be withdrawn by the pump 17 and circulated from the pipe 13 to the second tank 4 through the pipes 14, 15 a, 15 b and 15 c.

一方、図3に示すように、原水の供給が、ポンプ11、切替手段5及び原水供給路12bを介して第2槽4に行われる場合には、第2槽4が、原水中に第2の担体層41を浸漬して生物処理する浸漬ろ床法により原水を処理する「浸漬ろ床槽」として機能し、第1槽3が、第2槽4で得られた処理水を、第1の担体層31の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能する。   On the other hand, as shown in FIG. 3, when the raw water is supplied to the second tank 4 via the pump 11, the switching means 5, and the raw water supply path 12b, the second tank 4 Functions as an “immersion filter tank” for treating raw water by the immersion filter method in which the carrier layer 41 is immersed and biologically treated, and the first tank 3 converts the treated water obtained in the second tank 4 into the first tank. Function as a "water sprinkling filter tank" for treating treated water by the sprinkling filter method of spraying from the upper part of the carrier layer 31 and biologically treating the treated water.

図3において、第1槽3から流出する処理水の一部は、ポンプ17により引き抜かれて、配管16a、16b及び15cを通って配管13から第1槽3に循環させてもよい。残りの処理水は、配管16a、16c、15a、14を通って処理水槽7へ送られる。   In FIG. 3, a part of the treated water flowing out of the first tank 3 may be withdrawn by the pump 17 and circulated from the pipe 13 to the first tank 3 through the pipes 16a, 16b and 15c. The remaining treated water is sent to the treated water tank 7 through the pipes 16a, 16c, 15a, and 14.

なお、本実施形態において「浸漬ろ床法(浸漬ろ床槽)」とは、処理流体(原水)中に担体を浸漬させて、槽の上方もしくは下方から処理流体を接触させることにより、担体の表面に生物膜を付着させた後、生物膜と処理流体とを接触させることにより処理流体を生物処理する方法(装置)を意味する。   In the present embodiment, the “immersion filtration method (immersion filtration tank)” refers to immersing a carrier in a treatment fluid (raw water) and bringing the treatment fluid into contact with the treatment fluid from above or below the vessel. It means a method (apparatus) for biologically treating a treatment fluid by contacting the biofilm with the treatment fluid after attaching the biofilm to the surface.

浸漬ろ床法により処理流体を処理する際は、空気を吹き込まずに嫌気性固定床として運転することも、ブロワ等で空気を吹き込んで好気性固定床として運転することもできる。浸漬ろ床槽に設置されるブロワをタイマーで切り替えることにより、嫌気と好気を切り替えることもできる。図5及び図6に示すように、浸漬ろ床槽が2槽以上ある場合には、一部の槽を嫌気性固定床、残りの槽を好気性固定床として運転することもできる。処理流体の通水方向も、上向流、下向流のいずれの方式も採用できるが、散水ろ床との組み合わせから考えると、上向流浸漬ろ床方式が好ましい。   When the treatment fluid is treated by the immersion filter bed method, it can be operated as an anaerobic fixed bed without blowing air, or can be operated as an aerobic fixed bed by blowing air with a blower or the like. It is also possible to switch between anaerobic and aerobic by switching the blower installed in the immersion filter tank with a timer. As shown in FIGS. 5 and 6, when there are two or more immersion filter tanks, some tanks can be operated as an anaerobic fixed bed and the remaining tanks can be operated as an aerobic fixed bed. The flow direction of the processing fluid may be any of an upward flow and a downward flow. However, considering the combination with the sprinkling filter, the upward flow immersion filter is preferable.

浸漬ろ床を好気式とした場合は、嫌気式に比べて有機物の除去及び硝化を促進させることができる。浸漬ろ床を曝気する場合は、浸漬ろ床中のDOが0.5mg/L以上となるように曝気風量を制御することが好ましい。この曝気風量は、空洗(ろ床の流動によるろ床の洗浄を目的した曝気)ではないため、一般的な空洗時の曝気流量(50〜60m3/m2/h(上水の高速ろ過の逆洗時の空気量))に比べて、その曝気風量は僅かでよく、曝気に必要な動力を低減できる。 When the immersion filter bed is of the aerobic type, removal of organic substances and nitrification can be promoted as compared with the anaerobic type. When aerating the immersion filter bed, it is preferable to control the amount of aeration air so that DO in the immersion filter bed becomes 0.5 mg / L or more. Since this aeration air volume is not an air washing (aeration for the purpose of washing the filter bed by the flow of the filter bed), a general aeration flow at the time of the air washing (50 to 60 m 3 / m 2 / h (high-speed water supply) The amount of air to be aerated may be small compared to the amount of air during backwashing of filtration)), and the power required for aeration can be reduced.

浸漬ろ床を嫌気式とした場合には、脱窒反応が促進される。脱窒反応を促進させるためには、有機物および硝酸態窒素が必要なため、浸漬ろ床槽の後段に接続される散水ろ床槽で得られる処理水を浸漬ろ床槽側に循環させることが好ましい。   When the immersion filter bed is an anaerobic type, the denitrification reaction is promoted. In order to promote the denitrification reaction, organic matter and nitrate nitrogen are required, so that the treated water obtained in the sprinkling filter tank connected to the latter stage of the immersion filter tank can be circulated to the immersion filter tank side. preferable.

本実施形態における「散水ろ床法(散水ろ床槽)」とは、処理流体(原水)を、ろ床上部から散布して、ろ床を構成する単体の表面に生物膜を付着させた後、装置上部から下方へと流れる処理流体と生物膜とを接触させることにより、処理流体を生物処理する方法(装置)を意味する。散水ろ床法を長時間実施することにより、ろ床を構成する担体層の表面には汚泥が付着し、付着した汚泥が腐敗することにより悪臭が発生する。或いは、この汚泥に起因して、ろ床バエとよばれるチョウバエの一種が発生する。   The “watering filter method (watering filter tank)” in the present embodiment refers to a method in which a treatment fluid (raw water) is sprayed from the upper part of a filter bed and a biofilm is attached to a surface of a simple substance constituting the filter bed. Means a method (apparatus) for biologically treating a processing fluid by contacting the biological fluid with a processing fluid flowing downward from the top of the apparatus. By performing the trickling filter method for a long time, sludge adheres to the surface of the carrier layer constituting the filter bed, and the adhered sludge rots, thereby generating an odor. Alternatively, due to the sludge, a kind of butterfly fly called filter fly is generated.

切替手段5は、切替弁等で構成され、図1に示すように、第1槽3に原水を供給する配管12aと第2槽4に原水を供給する配管12bに接続されている。切替手段5は、制御手段6に電気的に接続されることができ、制御手段6からの制御信号を受けて、原水の供給を第1槽3側から第2槽4側へ、又は第2槽4側から第1槽3側へと切り替えることができる。   The switching means 5 includes a switching valve and the like, and is connected to a pipe 12a for supplying raw water to the first tank 3 and a pipe 12b for supplying raw water to the second tank 4, as shown in FIG. The switching means 5 can be electrically connected to the control means 6 and receives the control signal from the control means 6 to supply the raw water from the first tank 3 to the second tank 4 or the second tank 4. It is possible to switch from the tank 4 side to the first tank 3 side.

制御手段6は、散水ろ床法により処理される側の槽の汚染具合に基づいて、切替手段5による切替操作(切替のタイミング)を制御するように構成される。散水ろ床法の汚染具合が所定の条件を満足した場合に制御手段6が切替手段5を切り替えることで、原水の供給を、浸漬ろ床槽側から散水ろ床槽側へと切り替える。これにより、散水ろ床槽内に原水を流入させて散水ろ床槽内を原水で満たして散水ろ床槽を洗浄することが可能になるとともに、散水ろ床槽の洗浄水は、浸漬ろ床槽側へ供給して生物処理することが可能になる。その結果、水処理装置の運転を停止させることなく効率良く悪臭及びろ床バエの発生を抑制可能となる。なお、操作者が手動で切替手段5による切替を行ってもよいことは勿論である。   The control means 6 is configured to control the switching operation (switching timing) by the switching means 5 based on the degree of contamination of the tank to be treated by the trickling filter method. When the degree of contamination in the trickling filter method satisfies a predetermined condition, the control means 6 switches the switching means 5 to switch the supply of raw water from the immersion filter tank to the trickle filter tank. This allows the raw water to flow into the sprinkling filter tank to fill the sprinkling filter tank with raw water and wash the sprinkling filter tank, and the washing water in the sprinkling filter tank is immersed in the filter tank. It can be supplied to the tank side for biological treatment. As a result, it is possible to efficiently suppress the generation of offensive odor and filter bed fly without stopping the operation of the water treatment apparatus. In addition, it is a matter of course that the operator may manually perform the switching by the switching unit 5.

切替手段5による切替のタイミングとしては、以下に制限されるものではないが、例えば以下の指標に基づくことができる。   The timing of switching by the switching means 5 is not limited to the following, but can be based on, for example, the following indices.

(1)処理水スクリーンの固形物捕捉量
図4に示すように、第1槽3及び第2槽4の処理出口にそれぞれ目幅0.5〜2mm程度のスクリーン32、42を配置する。このスクリーン32、42には、処理が進むにつれて固形物が捕捉されるため、捕捉された固形物中にろ床バエの幼虫、蛹、成虫が観察された場合に、散水ろ床法により処理される側の槽の汚染具合が進んでいると判断し、切替手段5による原水の供給方向の切替を実施する。スクリーン32、42上に捕捉される固形物の確認は操作者が目視で行ってもよいし、例えばカメラ等の検出手段に基づいて、制御手段6が自動的に判断して切替手段5による切替動作を制御するようにしてもよい。
(1) Amount of Solids Captured by Treated Water Screen As shown in FIG. 4, screens 32 and 42 each having a mesh width of about 0.5 to 2 mm are arranged at the processing outlets of the first tank 3 and the second tank 4. Since solids are captured on the screens 32 and 42 as the processing proceeds, if larvae, pupae, or adults of filter fly are observed in the captured solids, the screens are treated by the sprinkling filter method. It is determined that the degree of contamination of the tank on the other side is advanced, and the switching direction of the raw water supply is switched by the switching means 5. The confirmation of the solid matter captured on the screens 32 and 42 may be visually performed by the operator, or automatically performed by the control means 6 based on detection means such as a camera, and switched by the switching means 5. The operation may be controlled.

(2)一定期間毎に運転切替
ろ床バエの成長に基づく所定の期間毎に定期的に運転切替する方法であり、3〜30日のいずれかの期間で定期的に運転切替することが好ましい。ろ床バエの幼虫は汚泥(スライム状の微生物塊)を餌として成長する。成長の速度は気温等により異なるが、一般的に卵2日、幼虫9〜15日、蛹2〜4日で成虫となり、成虫の生存期間は4〜14日とされる。卵が孵化するまでが3日、卵がろ床に付着してから成虫となり、さらに卵を産むまでが約30日であることから、3日で切り替えると卵が孵化すること自体を防止でき、30日で切り替えると卵が付着した場合一旦成虫まで成長するものの、その成虫が産んだ卵が孵化することを防ぐことができる。
(2) Switching operation every certain period This is a method of periodically switching the operation every predetermined period based on the growth of filter fly, and it is preferable to switch the operation periodically in any period of 3 to 30 days. . The larvae of the filter fly grow on sludge (slime-like microbial clumps). The growth speed varies depending on the temperature and the like, but generally, the eggs become adults after 2 days of eggs, 9 to 15 days of larvae, and 2 to 4 days of pupae, and the survival period of adults is 4 to 14 days. Eggs hatch for three days, eggs attach to the filter bed and become adults, and since it takes about 30 days to lay eggs, switching to three days can prevent the eggs from hatching itself, If the eggs are attached after switching for 30 days, the eggs once grow to adults, but the eggs laid by the adults can be prevented from hatching.

(3)担体付着生物量
第1の担体層31又は第2の担体層41に付着する担体付着生物量に基づいて、運転切替する方法である。担体に付着した生物量(担体付着生物量)が、担体を充填した有効容量あたりの3000〜6000mg−SS/L以上なると、担体付着生物量が多くなり、ろ材閉塞を生じ、ハエの発生しやすい環境になる。そのため、担体付着生物量が3000〜6000mg−SS/Lとなった場合に、操作者又は制御手段6が、散水ろ床法により処理される側の槽の汚染具合が進んでいると判断し、切替手段5による原水の供給の切替を実施するものである。
(3) Amount of living organisms adhered to carrier This is a method of switching operation based on the amount of organisms adhered to the first carrier layer 31 or the second carrier layer 41. When the amount of organisms attached to the carrier (the amount of organisms attached to the carrier) is 3000 to 6000 mg-SS / L or more per the effective volume of the filled carrier, the amount of organisms attached to the carrier increases, the filter medium becomes blocked, and flies easily occur. Environment. Therefore, when the amount of organisms attached to the carrier becomes 3000 to 6000 mg-SS / L, the operator or the control means 6 determines that the degree of contamination of the tank to be treated by the trickling filter method is advanced, The switching of the supply of the raw water by the switching means 5 is performed.

担体付着生物量の測定方法としては、反応槽から所定量のろ材(砕石等の一つ一つ分けられるものについては個数、ろ布のように分けられない場合は所定の面積)を採取し、ろ材に付着した生物膜を剥離させた後、生物膜のSS量を測定する。反応槽に投入した担体量からおよび所定量のろ材に付着した生物膜のSS量より、反応槽の有効容積あたりの生物量を算出することが可能である。   As a method for measuring the amount of organisms attached to the carrier, a predetermined amount of a filter medium (the number of pieces that can be separated one by one such as crushed stones, and a predetermined area if they cannot be separated like a filter cloth) are collected from a reaction tank, After removing the biofilm attached to the filter medium, the SS amount of the biofilm is measured. The biomass per effective volume of the reaction tank can be calculated from the amount of the carrier charged into the reaction tank and the SS amount of the biofilm attached to a predetermined amount of the filter medium.

担体付着生物量の測定は、所定のタイミングで担体の一部をサンプリングすることにより行い、担体付着生物量が3000〜6000mg−SS/L以上となる所要期間を算出し、その所要期間に基づいて切替手段5による切替を実施するようにしてもよい。   The measurement of the amount of organisms attached to the carrier is performed by sampling a part of the carrier at a predetermined timing, and a required period in which the amount of organisms attached to the carrier is 3000 to 6000 mg-SS / L or more is calculated. Switching by the switching means 5 may be performed.

このように、本発明の実施の形態に係る水処理装置及び水処理方法によれば、切替手段5が原水の流入配管である原水供給路12a、12bを切り替えることで、装置の運転を長時間止めることなく、散水ろ床を冠水させることが可能になる。そのため、散水ろ床からの悪臭、ろ床バエの発生を長期的に防ぐことができ、装置の維持管理が容易になる。また、散水ろ床槽の運転を止めてろ床を洗浄処理する従来の手法と比べて、散水ろ床の洗浄排水用の配管やポンプ等の機器が不要となることから、コストおよび装置の設置面積の削減にも繋がる。更に、散水ろ床の洗浄時に生じた洗浄排水も、後段の槽で連続的に生物処理することが可能であるため、高濃度の洗浄排水を排出しなくて済む。   As described above, according to the water treatment apparatus and the water treatment method according to the embodiment of the present invention, the switching unit 5 switches the raw water supply paths 12a and 12b, which are the raw water inflow pipes, so that the operation of the apparatus can be performed for a long time. Without stopping, the watering filter can be flooded. Therefore, it is possible to prevent the generation of offensive odor and filter flies from the sprinkling filter for a long time, and the maintenance and management of the apparatus becomes easy. Also, compared to the conventional method of stopping the operation of the trickling filter bed and cleaning the filter bed, equipment such as pipes and pumps for washing and draining the trickling filter bed is not required, so that the cost and the installation area of the device are reduced. It also leads to reduction of Further, the washing wastewater generated at the time of washing the sprinkling filter bed can be continuously biologically treated in a later tank, so that it is not necessary to discharge the washing wastewater of high concentration.

(4)変形例
図5及び図6に示すように、第1槽3及び第2槽4と同様に、散水ろ床式装置と浸漬ろ床式装置の機能を両立する反応槽(第3槽8及び第4槽9)を更に直列に配置することも可能である。例えば、図5に示すように、原水の供給が、ポンプ11及び切替手段5及び原水供給路12aを介して第1槽3に行われる場合には、第1槽3が、原水中に第1の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理する「浸漬ろ床槽」として機能し、第2槽4が、第1槽3で得られた処理水を第2の担体層の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能し、第3槽8が、第2槽4で得られた処理水中に第3の担体層81を浸漬して生物処理する浸漬ろ床法により処理水をを処理する「浸漬ろ床槽」として機能し、第4槽9が、第3槽8で得られた処理水を第4の担体層91の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能する。
(4) Modification As shown in FIGS. 5 and 6, similarly to the first tank 3 and the second tank 4, a reaction tank (third tank) having both functions of a trickling filter type apparatus and a submerged filter type apparatus. 8 and the fourth tank 9) can also be arranged in series. For example, as shown in FIG. 5, when the raw water is supplied to the first tank 3 via the pump 11, the switching means 5, and the raw water supply path 12a, the first tank 3 Functions as an "immersion filter tank" for treating raw water by the immersion filter method in which the carrier layer is immersed and biologically treated, and the second tank 4 uses the treated water obtained in the first tank 3 as a second carrier. The third tank 8 functions as a "watering filter tank" for treating the treated water by the sprinkling filter method of spraying from the upper part of the layer and biologically treating the treated water. The fourth tank 9 functions as a “immersion filter tank” for treating the treated water by the immersion filter bed method in which the carrier layer 81 is immersed and biologically treated, and the fourth tank 9 transfers the treated water obtained in the third tank 8 to the fourth tank 8. Function as a "water sprinkling filter tank" for treating the treated water by the sprinkling filter method of spraying from the upper part of the carrier layer 91 and biologically treating it.

一方、図6に示すように、原水の供給が、ポンプ11、切替手段5及び原水供給路12bを介して第4槽9に行われる場合には、第4槽9が、原水中に第4の担体層91を浸漬して生物処理する浸漬ろ床法により原水を処理する「浸漬ろ床槽」として機能し、第3槽8が、第4槽9で得られた処理水を、第3の担体層81の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能し、第2槽4が、第3槽8で得られた処理水中に第2の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理する「浸漬ろ床槽」として機能し、第1槽3が、第2槽4で得られた処理水を、第1の担体層の上部から散布して生物処理する散水ろ床法により処理水を処理する「散水ろ床槽」として機能する。このように、反応槽の個数は偶数単位で増設することが可能である。   On the other hand, as shown in FIG. 6, when the raw water is supplied to the fourth tank 9 via the pump 11, the switching means 5, and the raw water supply path 12b, the fourth tank 9 Functions as an “immersion filter tank” in which raw water is treated by the immersion filter method in which the carrier layer 91 is immersed and biologically treated, and the third tank 8 converts the treated water obtained in the fourth tank 9 into the third tank. The second tank 4 functions as a "watering filter tank" for treating the treated water by the sprinkling filter method of spraying from the upper part of the carrier layer 81 and biologically treating the treated water. The first tank 3 functions as a “immersion filter tank” in which raw water is treated by the immersion filter method in which the second carrier layer is immersed and biologically treated. It functions as a "sprinkling filter tank" for treating treated water by the trickling filter method of spraying from the upper part of the carrier layer and biologically treating it. As described above, the number of reaction vessels can be increased in even units.

図7及び図8に示すように、散水ろ床槽の後段の浸漬ろ床槽を、上向流の浸漬ろ床とすることで、浸漬ろ床に固液分離槽としての機能を持たせることも可能である。この場合でも、上述の実施形態と同様に、制御手段6により流路を切り替えることで、定期的にろ床を浸漬させ、ろ床バエの発生を防止することが可能である。図7及び図8に示す装置によれば、浸漬ろ床槽側には原水に含まれるSS成分やろ床から剥離した生物膜が固液分離される。浸漬ろ床に蓄積した汚泥は、定期的に引抜を行い汚泥量を調整する。この操作により、処理水中のSS濃度を低減させることが可能になる。   As shown in FIG. 7 and FIG. 8, the dipping filter bed at the subsequent stage of the sprinkling filter tank is an upflow dipping filter bed so that the dipping filter bed has a function as a solid-liquid separation tank. Is also possible. Also in this case, similarly to the above-described embodiment, by switching the flow path by the control means 6, the filter bed can be immersed periodically to prevent the generation of filter bed flies. According to the apparatus shown in FIGS. 7 and 8, the SS component contained in the raw water and the biofilm separated from the filter bed are separated into solid and liquid on the immersion filter bed tank side. The sludge accumulated in the immersion filter bed is periodically pulled out to adjust the amount of sludge. This operation makes it possible to reduce the SS concentration in the treated water.

(5)水処理システム
本発明の実施の形態に係る水処理装置は、図9(a)〜図9(g)に示すような水処理システムに組み込むことができる。図9(a)〜図9(d)に示す「前段固液分離」装置としては、スクリーン、沈殿池、ろ過装置等が考えられ、原水に含まれるSS成分の量および性質により選定する。図9(a)に示すシステムは、最も単純なシステムであり、前段固液分離により夾雑物を除去した後、本発明の実施の形態に係る水処理装置(本装置)で処理し、処理水を放流するものである。図9(b)及び図9(c)に示すように、本発明の実施の形態に係る水処理装置の後段に最終沈殿池又は生物ろ過装置などの固液分離装置を設けて処理水中のSS成分を分離するシステム、図9(d)に示すように、本発明の実施の形態に係る水処理装置の後段に曝気槽と固液分離槽を設けるシステムであってもよい。或いは、図9(e)〜図9(g)に示すように、本発明の実施の形態に係る水処理装置の前段にUASB(Up−flow Anaerobic Sludge Blanket)を設け、原水を予め嫌気的に処理するシステムにも好適に用いられる。
(5) Water Treatment System The water treatment apparatus according to the embodiment of the present invention can be incorporated in a water treatment system as shown in FIGS. 9 (a) to 9 (g). Screens, sedimentation basins, filtration devices, and the like are considered as the "pre-solid-liquid separation" device shown in FIGS. 9A to 9D, and are selected according to the amount and properties of the SS component contained in the raw water. The system shown in FIG. 9A is the simplest system. After removing impurities by solid-liquid separation in the first stage, the system is treated with the water treatment apparatus (the present apparatus) according to the embodiment of the present invention, and treated water is treated. Is released. As shown in FIG. 9 (b) and FIG. 9 (c), a solid-liquid separation device such as a final sedimentation basin or a biological filtration device is provided at the subsequent stage of the water treatment device according to the embodiment of the present invention, and SS in the treated water is provided. A system for separating components, as shown in FIG. 9 (d), may be a system in which an aeration tank and a solid-liquid separation tank are provided after the water treatment apparatus according to the embodiment of the present invention. Alternatively, as shown in FIG. 9 (e) to FIG. 9 (g), a UASB (Up-flow Anaerobic Sludge Blanket) is provided in front of the water treatment apparatus according to the embodiment of the present invention, and raw water is anaerobically prepared in advance. It is also suitably used for processing systems.

本発明の実施の形態に係る水処理装置は、既存の水処理システムに対して設備増強的に用いることもできる。例えば、図10(a)に示すように、既設の最初沈殿池で得られる処理水を本実施形態に係る水処理装置に引き込み処理した後、処理水を既設の最終沈殿池へ返送することもできる。或いは図10(b)に示すように、既設の最初沈殿池で得られる処理水を本実施形態に係る水処理装置に引き込み処理した後、曝気槽に返送することもできる。   The water treatment apparatus according to the embodiment of the present invention can also be used for existing water treatment systems in a facility-enhancing manner. For example, as shown in FIG. 10A, the treated water obtained in the existing first sedimentation basin is drawn into the water treatment apparatus according to the present embodiment, and the treated water is returned to the existing final sedimentation basin. it can. Alternatively, as shown in FIG. 10B, the treated water obtained in the existing first sedimentation basin may be drawn into the water treatment apparatus according to the present embodiment, and then returned to the aeration tank.

このように、本発明は上記の開示から妥当な特許請求の範囲の発明特定事項によって表されるものであり、実施段階においては、その要旨を逸脱しない範囲において変形し具体化し得るものである。   As described above, the present invention is represented by the invention specifying matters appropriate in the claims based on the above disclosure, and can be modified and embodied in the execution stage without departing from the gist thereof.

以下に本発明の実施例を比較例と共に示すが、これらの実施例は本発明及びその利点をよりよく理解するために提供するものであり、発明が限定されることを意図するものではない。   Hereinafter, Examples of the present invention are shown together with Comparative Examples, but these Examples are provided for better understanding of the present invention and its advantages, and are not intended to limit the invention.

(実施例1)
図1で示す水処理装置を用いて水処理を実施した。原水は人工下水(グルコース160mg/L、ペプトン160mg/L、リン酸一カリウム12mg/L)を用いた。原水の成分は、BOD250mg/L、CODCr370mg/Lであった。ろ材は第1槽、第2槽ともにポリプロピレン製の担体を充填し、充填部の寸法はL200mm×D200mm×H860mmであり、ろ材充填部の容量は34.4Lとした。下水処理場の余剰汚泥を循環運転によりろ材に接触させた後、上記人工下水を原水とし、BOD容積負荷0.05〜2.3kg−BOD/m3/dの範囲で段階的に負荷を上げて運転することでろ材に生物を馴致させた(図11)。馴致後はBOD容積負荷2.3kg−BOD/m3/dで運転を行った。散水ろ床槽における散水負荷が40m3/m2/dとなるように処理水の一部を循環させた。散水ろ床の散水部は、多孔板によりろ床全体に散水させた。
(Example 1)
Water treatment was performed using the water treatment device shown in FIG. As raw water, artificial sewage (glucose 160 mg / L, peptone 160 mg / L, monopotassium phosphate 12 mg / L) was used. The components of the raw water were BOD 250 mg / L and CODCr 370 mg / L. The filter medium was filled with a carrier made of polypropylene in both the first tank and the second tank. The dimensions of the filled portion were L200 mm x D200 mm x H860 mm, and the capacity of the filter material filled portion was 34.4 L. After the excess sludge of the sewage treatment plant is brought into contact with the filter medium by circulation operation, the artificial sewage is used as raw water, and the load is increased stepwise in the range of 0.05 to 2.3 kg-BOD / m 3 / d of BOD volume load. The organism was made to acclimate to the filter medium by operating the filter medium (FIG. 11). After the adaptation, the operation was performed at a BOD volume load of 2.3 kg-BOD / m 3 / d. Part of the treated water was circulated such that the watering load in the watering filter tank became 40 m 3 / m 2 / d. The sprinkling part of the sprinkling filter bed was sprinkled over the entire filter bed with a perforated plate.

表1に装置運転状況(切替状況)を示す。実施例1では、1週間ごとにラインの切替を行い、散水ろ床槽と浸漬ろ床槽の切替を行った。実施例2では2週間ごとにラインの切替を行った。実施例3では1ヶ月ごとにラインの切替を行った。それぞれの実施期間は、実施例1〜3それぞれに対し、4週間、4週間、8週間とした。比較例では、図1で示す水処理装置において、排水、担体、装置の運転負荷については実施例1と同様としたが、ラインの切替を行わなかった。   Table 1 shows the device operation status (switching status). In Example 1, the line was switched every week, and the watering filter tank and the immersion filter tank were switched. In Example 2, the line was switched every two weeks. In Example 3, the line was switched every month. The respective execution periods were set to four weeks, four weeks, and eight weeks for Examples 1 to 3, respectively. In the comparative example, in the water treatment apparatus shown in FIG. 1, the drainage, the carrier, and the operation load of the apparatus were the same as those in Example 1, but the line was not switched.

Figure 0006652898
Figure 0006652898

実施例1〜3及び比較例におけるろ床バエの発生状況を表2に示す。表2に示すように、実施例1、2ではろ床バエは全く確認されなかった。実施例3では第2槽において散水ろ床運転時にろ床バエの発生がみられたが、運転切替後にはろ床バエの発生が確認されなくなった。比較例では、運転20日目に第2槽の散水ろ床部にてろ床バエの発生が確認され、その後ろ床バエおよびその幼虫は実験を終えた120日目まで発生を続けた。   Table 2 shows the occurrence of filter bed flies in Examples 1 to 3 and Comparative Example. As shown in Table 2, no filter flies were observed in Examples 1 and 2. In Example 3, the generation of filter bed flies was observed in the second tank during the sprinkling filter operation, but the occurrence of filter bed flies was not confirmed after the operation was switched. In the comparative example, on the 20th day of operation, the occurrence of filter fly was confirmed in the sprinkling filter section of the second tank, and the rear fly and its larva continued to develop until the 120th day after the experiment was completed.

Figure 0006652898
Figure 0006652898

1…原水槽
3…第1槽
4…第2槽
5…切替手段
6…制御手段
7…処理水槽
8…第3槽
9…第4槽
11…ポンプ
12a…原水供給路(配管)
12b…原水供給路(配管)
13…配管
14…配管
17…ポンプ
31…第1の担体層
32…スクリーン
41…第2の担体層
42…スクリーン
81…第3の担体層
91…第4の担体層
DESCRIPTION OF SYMBOLS 1 ... Raw water tank 3 ... 1st tank 4 ... 2nd tank 5 ... Switching means 6 ... Control means 7 ... Treatment water tank 8 ... 3rd tank 9 ... 4th tank 11 ... Pump 12a ... Raw water supply path (piping)
12b: Raw water supply path (piping)
DESCRIPTION OF SYMBOLS 13 ... Pipe 14 ... Pipe 17 ... Pump 31 ... 1st carrier layer 32 ... Screen 41 ... 2nd carrier layer 42 ... Screen 81 ... 3rd carrier layer 91 ... 4th carrier layer

Claims (7)

微生物を付着した第1の担体層を備える第1槽と、
前記第1槽の後段に接続され、微生物を付着した第2の担体層を備える第2槽と、
前記第1槽又は前記第2槽へ原水を供給可能な原水供給路と、
原水の供給を、前記第1槽と前記第2槽との間で切り替える切替手段とを備え、
前記切替手段が原水の供給を前記第1槽に切り替えることにより、前記第1槽が原水中に前記第1の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理し、前記第2槽が前記第1槽で得られた処理水を前記第2の担体層の上部から散布して生物処理する散水ろ床法により前記処理水を処理し、
前記切替手段が原水の供給を前記第2槽に切り替えることにより、前記第2槽が原水中に前記第2の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理し、前記第1槽が前記第2槽で得られた処理水を前記第1の担体層の上部から散布して生物処理する散水ろ床法により前記処理水を処理し、
前記切替手段が、散水ろ床法により処理される側の槽の汚染具合に基づいて、前記第1槽と前記第2槽との間で交互に切り替えることを特徴とする水処理装置。
A first tank having a first carrier layer to which microorganisms are attached;
A second tank connected to the subsequent stage of the first tank and including a second carrier layer to which microorganisms are attached;
A raw water supply passage capable of supplying raw water to the first tank or the second tank;
Supply of raw water, and a switching means for switching between said second vessel and said first vessel,
The switching means switches the supply of the raw water to the first tank, so that the first tank treats the raw water by an immersion filter method in which the first carrier layer is immersed in the raw water and biologically treated. Two tanks treat the treated water by a trickling filter method in which the treated water obtained in the first tank is sprayed from above the second carrier layer and subjected to biological treatment,
The switching means switches the supply of the raw water to the second tank, whereby the second tank treats the raw water by an immersion filter method in which the second carrier layer is immersed in the raw water and biologically treated. 1 tank treats the treated water by a sprinkling filter method in which treated water obtained in the second tank is sprayed from above the first carrier layer and subjected to biological treatment ,
A water treatment apparatus , wherein the switching means alternately switches between the first tank and the second tank based on the degree of contamination of the tank to be treated by the trickling filter method .
前記切替手段が、ろ床バエの成長を考慮した所定の期間毎に、原水の切り替えを行うことを含む請求項1に記載の水処理装置。The water treatment apparatus according to claim 1, wherein the switching unit switches the raw water every predetermined period in consideration of the growth of the filter fly. 前記原水供給路が、前記第1槽及び前記第2槽の下方に接続され、前記第1槽又は前記第2槽の下方から原水を上向流で通水することを含む請求項1又は2に記載の水処理装置。The said raw water supply path is connected below the said 1st tank and the said 2nd tank, and includes flowing raw water by an upward flow from under the said 1st tank or the said 2nd tank. A water treatment apparatus according to item 1. 前記第1槽及び前記第2槽の処理水出口に配置されたスクリーンと、
記スクリーンに捕捉された固形物量に基づいて、前記切替手段を制御する制御手段と、
備える請求項1〜3のいずれか1項に記載の水処理装置。
A screen disposed at a treated water outlet of the first tank and the second tank ;
Based on the captured solid content before Symbol screen, and control means for controlling said switching means,
Water treatment device according to claim 1 comprising a.
前記第1の担体層又は前記第2の担体層に付着する担体付着生物量に基づいて、前記切替手段を制御する制御手段を備える請求項1〜4のいずれか1項に記載の水処理装置。 The water treatment apparatus according to any one of claims 1 to 4 , further comprising a control unit that controls the switching unit based on a biomass of the carrier adhered to the first carrier layer or the second carrier layer. . 微生物を付着した第1の担体層を原水に浸漬して生物処理する浸漬ろ床槽と、
微生物を付着した第2の担体層を備え、前記浸漬ろ床槽からの処理水を、前記第2の担体層の上部から散布して接触させることにより生物処理する散水ろ床槽と、
原水を前記浸漬ろ床槽又は前記散水ろ床槽へ供給するための原水供給路と、
前記散水ろ床槽の汚染具合に基づいて、原水の供給を前記浸漬ろ床槽側又は前記散水ろ床槽側へと交互に切り替える切替手段と
を備え、
前記切替手段が、原水の供給を前記浸漬ろ床槽側から前記散水ろ床槽側へと切り替えることにより、前記散水ろ床槽内に原水を流入させて前記散水ろ床槽内を原水で満たして前記散水ろ床槽を洗浄するとともに、前記散水ろ床槽の洗浄水を前記浸漬ろ床槽側へ供給して生物処理することを特徴とする水処理装置。
An immersion filter tank for biological treatment by immersing the first carrier layer to which microorganisms are attached in raw water;
A sprinkling filter tank provided with a second carrier layer to which microorganisms are attached, and treated water from the immersion filter bed tank is subjected to biological treatment by spraying and contacting the water from the upper portion of the second carrier layer,
Raw water supply path for supplying raw water to the immersion filter tank or the sprinkling filter tank,
Switching means for alternately switching the supply of raw water to the immersion filter tank side or to the trickle filter tank side , based on the degree of contamination of the trickling filter tank,
The switching means switches the supply of raw water from the immersion filter tank to the sprinkle filter tank so that raw water flows into the sprinkler filter tank and fills the sprinkler filter tank with raw water. A water treatment apparatus for washing the sprinkling filter tank with the washing water and supplying the washing water of the sprinkling filter tank to the immersion filter tank side for biological treatment.
微生物を付着した第1の担体層を備える第1槽に原水を供給し、前記第1槽において原水中に前記第1の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理するとともに、前記第1槽の後段に接続され、微生物を付着した第2の担体層を備える第2槽において、前記第1槽で得られた処理水を前記第2の担体層の上部から散布して生物処理する散水ろ床法により前記処理水を処理することと、
原水を前記第1槽から前記第2槽へ供給するように切り替えることと、
前記第2槽において原水中に前記第2の担体層を浸漬して生物処理する浸漬ろ床法により原水を処理するとともに、前記第1槽において、前記第2槽で得られた処理水を前記第1の担体層の上部から散布して生物処理する散水ろ床法により処理することと、
散水ろ床法により処理される側の槽の汚染具合に基づいて、前記第1槽と前記第2槽との間で交互に切り替えること
を含む水処理方法。
Raw water is supplied to a first tank provided with a first carrier layer to which microorganisms are adhered, and the raw water is treated by the immersion filter bed method in which the first carrier layer is immersed in the raw water in the first tank and biologically treated. At the same time, in the second tank connected to the subsequent stage of the first tank and provided with the second carrier layer to which the microorganisms are attached, the treated water obtained in the first tank is sprayed from above the second carrier layer. Treating the treated water by a sprinkling filter method of biological treatment,
Switching to supply raw water from the first tank to the second tank;
The raw water is treated by the immersion filter method of immersing the second carrier layer in the raw water in the second tank and biologically treating the raw water, and in the first tank, the treated water obtained in the second tank is subjected to the treatment. Spraying from the upper part of the first carrier layer and treating by a trickling filter method for biological treatment ;
A water treatment method comprising: alternately switching between the first tank and the second tank based on the degree of contamination of the tank to be treated by the trickling filter method.
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