JP3230742U - Water purification equipment - Google Patents

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JP3230742U
JP3230742U JP2020001264U JP2020001264U JP3230742U JP 3230742 U JP3230742 U JP 3230742U JP 2020001264 U JP2020001264 U JP 2020001264U JP 2020001264 U JP2020001264 U JP 2020001264U JP 3230742 U JP3230742 U JP 3230742U
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田村善胤
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田村 善胤
田村 善胤
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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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Abstract

【課題】生物処理による浄化法(浄水処理法)の原理を用いながらも省スペースにし、しかも生物膜の管理を省力化し、ろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し浄水処理の安全性を確実にさせる、浄水処理装置を提供する。【解決手段】容器状の縦型枠組構造体3の外面に微生物が生息して構成される生物膜と、該縦型枠組構造体3内に収納したろ材層に微生物が生息して構成される生物膜と、更に濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水中に浮遊して流動状態で多数存在する多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜と、を有し、処理水または原水を接触させるとともに、ろ過池Gの水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)6を設けた。【選択図】図3PROBLEM TO BE SOLVED: To save space while using the principle of a purification method by biological treatment (water purification treatment method), to save labor in managing biological membranes, and to add a microporous physical microfiltration treatment step as the next step of a filtration pond. To provide a water purification device that ensures the safety of water purification treatment. SOLUTION: A biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure 3 and a filter medium layer housed in the vertical frame structure 3 inhabiting microorganisms. A carrier that serves as a biological residence formed of a biofilm and a large number of porous bodies suspended in raw water having a turbidity concentration of 10 mg / l or less or treated water that has been treated to further reduce turbidity. It has a biofilm composed of microorganisms inhabiting it, and it is in contact with treated water or raw water, and in the water of the filtration pond G, the vertical direction of the water can be arbitrarily selected, and an electrolysis device (electrolysis). Device) 6 was provided. [Selection diagram] Fig. 3

Description

本考案は水道水に含まれる水質的健康影響物質の低減を目的とし、特に原水処理のために注入添加される塩素剤として多用されている「次亜塩素ナトリウム」(有効塩素濃度は12%や6%)由来で混入するクロレートや、前駆物質と塩素により生じるトリハロメタン等の薬品由来の汚染物質、あるいは臭気物質等を可能な限り低減する水道原水の浄化処理法の汎用化を可能にする浄水処理装置に関するものである。
本考案の基本技術は英国のJシンプソン氏の発明(1800年代前半)による緩速生物ろ過法である。
このろ過法は水質的健康影響物質の低減、すなわち薬品無添加は基よりトータルとしての水処理コストも低減されるだけでなく、近年では原水に溶存するストロンチューム、セシウム等の除去効果も期待されることから、改めてその利便性が見直されている。
本考案は「緩速生物ろ過法」の浄水処理装置において、「省スペース化」、「省力化」、及び画期的に機能促進される可能性がある「緩速生物ろ過法」の浄水処理装置に関するものである。
The present invention aims to reduce water quality and health-affecting substances contained in tap water, and in particular, "sodium hypochlorite" (effective chlorine concentration is 12%), which is often used as a chlorine agent to be injected and added for raw water treatment. 6%) Water purification treatment that enables generalization of tap water purification treatment methods that reduce as much as possible chlorate mixed in, pollutants derived from chemicals such as trihalomethanes generated by precursors and chlorine, or odorous substances. It is about the device.
The basic technique of the present invention is a slow-speed biological filtration method invented by Mr. J Simpson of the United Kingdom (early 1800s).
This filtration method not only reduces the substances that affect water quality and health, that is, the addition of no chemicals reduces the total water treatment cost compared to the basics, but in recent years, it is expected to have the effect of removing strontium, cesium, etc. dissolved in raw water. Therefore, its convenience has been reviewed again.
The present invention is a "slow-speed biological filtration method" water purification device, "space-saving", "labor-saving", and "slow-speed biological filtration method" water purification treatment that may dramatically promote functions. It is about the device.

従来において上水道の浄化工程に薬品添加をしない浄化法(浄水処理法)として、微生物を活用する緩速ろ過法(1829年、シンプソン発明)が公知である。
これは粒径0.2〜0.4mm程度の砂を用いて深さ1.5m程度の砂層を有する池に、水道原水(浄化対象水)を砂層内流速4m/日程度で極めて緩やかに流せば砂層の表面に数時間で自然に生物膜が形成されて、対象水の浄化が始まり、多様な有害物質・病原性細菌・化学物質等を微生物の食物連鎖(硝化、脱窒、破砕分解、吸着、補足、変性、及びそれらの複合作用等)で自然消滅する自然浄化原理を用いた無理のない浄化法である。
この方法は要するに「Jシンプソンの緩速ろ過法」または「生物処理による浄化法(浄水処理法)」である。
自然に生成される前記生物膜の浄化作用は、各種微生物によるもので、また原生動物、藻類、水生生物の浄化作用も観られ、通過する原水に含まれる異物、溶存する有機物、臭気物質、鉄、アンモニア、マンガン、さらにはストロンチューム、セシウム等の除去にも効果があると期待される。
すなわち「生物処理による浄化法(浄水処理法)」は薬品無添加であるが故に薬品汚染を伴わないろ過法であり、ろ過時に塩素添加ゼロの浄水に、ろ過後において有効塩素を微量付与(給水末端で0.1mg/l程度の残留塩素を目標にすれば0.3mg/l程度の有効塩素の付与)すれば、日本の水道水で定められている二次汚染のリスクが少ない安全性の高い飲用水道水になる。
このような生物膜を用いた排水の処理装置として、例えば、下記特許文献1がある。
Conventionally, a slow sand filtration method (1829, Simpson invention) utilizing microorganisms is known as a purification method (water purification method) in which no chemical is added to the purification process of water supply.
This is done by using sand with a particle size of about 0.2 to 0.4 mm and pouring tap water (water to be purified) into a pond with a sand layer with a depth of about 1.5 m at a flow velocity of about 4 m / day in the sand layer. For example, a biological film is naturally formed on the surface of the sand layer in a few hours, purification of the target water begins, and various harmful substances, pathogenic bacteria, chemical substances, etc. are separated into the food chain of microorganisms (vitrification, denitrification, crushing and decomposition, It is a reasonable purification method using the principle of natural purification that disappears naturally by adsorption, supplementation, modification, and their combined action).
This method is, in short, "J Simpson's slow sand filtration method" or "biological treatment purification method (water purification method)".
The purifying action of the naturally generated biofilm is due to various microorganisms, and the purifying action of protozoa, algae, and aquatic organisms is also observed, and foreign substances, dissolved organic substances, odorous substances, and iron contained in the passing raw water are also observed. , Ammonia, manganese, as well as strontium, cesium, etc. are expected to be effective in removal.
In other words, the "purification method by biological treatment (water purification method)" is a filtration method that does not involve chemical contamination because it does not contain chemicals, and a small amount of effective chlorine is added to purified water with zero chlorine addition during filtration (water supply). If the target is residual chlorine of about 0.1 mg / l at the end, the effective chlorine of about 0.3 mg / l is added), and the risk of secondary contamination specified in tap water in Japan is low. It becomes expensive drinking tap water.
As a wastewater treatment device using such a biofilm, for example, there is the following Patent Document 1.

特開2019−34286号公報Japanese Unexamined Patent Publication No. 2019-34286

しかしこの方法は処理水量増大に比例して水面積(ろ過池の面積)が広大になると共に生物膜の管理に手間がかかるという問題がある。
一方現在用いられている浄化法(浄水処理法)は水面積(ろ過池の面積)が少ない(浄水場のスペースが少なくてすむ)急速ろ過法であり、この方法は運転操作を自動化することで省力的であることから広く用いられている。
しかし、この方法はあくまでも物理化学処理による浄化法(浄水処理法)であり前述の「生物処理による浄化法(浄水処理法)」とは異なり、特に塩素注入率が大きくなるため処理された水道水の薬品汚染(塩素由来の薬液汚染)のリスクが高いのである。
この急速ろ過法においては浄化対象水(原水)に酸化剤として塩素(Cl)を注入するが、この場合に対象水中のアンモニア態窒素の除去には条件にもよるが該アンモニア濃度の7倍以上(アンモニア濃度が1mg/lなら7mg/l以上)の濃度の塩素を注入しなければならないことになるので、どうしても過剰な塩素注入(消毒目的のための塩素量より格段に多い注入)となってしまう。過剰な塩素注入の結果、前駆物質との作用で塩素化合物(トリハロメタン等)が生成したり、異臭味等が生じたりして、浄水への悪影響を生じさせることになる。
However, this method has a problem that the water area (area of the filtration pond) becomes large in proportion to the increase in the amount of treated water and it takes time and effort to manage the biofilm.
On the other hand, the purification method (water purification method) currently used is a rapid filtration method in which the water area (area of the filtration pond) is small (the space of the water purification plant is small), and this method is by automating the operation operation. It is widely used because it is labor-saving.
However, this method is a purification method by physicochemical treatment (water purification method), and unlike the above-mentioned "purification method by biological treatment (water purification method)", tap water treated because the chlorine injection rate is particularly large. There is a high risk of chemical contamination (chlorine-derived chemical contamination).
In this rapid filtration method, chlorine (Cl 2 ) is injected into the purification target water (raw water) as an oxidizing agent. In this case, the removal of ammonia nitrogen in the target water is 7 times the ammonia concentration, depending on the conditions. Since it is necessary to inject chlorine with a concentration of the above (7 mg / l or more if the ammonia concentration is 1 mg / l), excessive chlorine injection (injection much larger than the amount of chlorine for disinfection purposes) is inevitable. It ends up. As a result of excessive chlorine injection, chlorine compounds (trihalomethane, etc.) are generated by the action with the precursor, and a strange odor is generated, which causes an adverse effect on purified water.

一方日本において厚生労働省は「薬品由来の汚染物質の混入を低減すべきことであること及び次亜塩素酸ナトリウムが本質的に分解性のある物質であることに配慮し」としており、これは「塩素導入率の低減」が望まれている、と解釈できる。
これに関して急速ろ過法において、異臭味対策でオゾン処理を急速ろ過池の前段後段に追加し塩素注入率を低減した事例もあるが、その設備コスト、維持管理コスト、施設更新時のコスト、電力消費費用、消耗品費用等を考慮すれば極めて不経済で、しかも環境負荷を増大させるという問題も生じさせている。
On the other hand, in Japan, the Ministry of Health, Labor and Welfare has stated that "consideration should be made to reduce the contamination of chemical-derived pollutants and that sodium hypochlorite is an essentially degradable substance." It can be interpreted that "reduction of chlorine introduction rate" is desired.
Regarding this, in the rapid sand filter method, there are cases where ozone treatment was added to the front and rear stages of the rapid sand filter to reduce the chlorine injection rate as a countermeasure against offensive odors, but the equipment cost, maintenance cost, facility renewal cost, and power consumption Considering the cost and the cost of consumables, it is extremely uneconomical and also causes a problem of increasing the environmental load.

本考案の第1の目的は「Jシンプソンの緩速ろ過法」または「生物処理による浄化法(浄水処理法)」の原理を用いながらも省スペースにすることであり、本考案の第2の目的は生物膜の管理の省力化であり、本考案の第3の目的はろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し浄水処理の安全性を確実にさせる、以上の3つを目的とする。
以上の3つの目的について以下分説する:
本考案の第1の目的は、上記の従来の急速ろ過法の問題点を解決すべく、「生物処理による浄化法(浄水処理法)」の原理を用い、それを構造的に改良して「生物処理による浄化法(浄水処理法)」のさらなる実用化を図るものである。
すなわちその改良点とは、従来の「生物処理による浄化法(浄水処理法)」においては「ろ過水量」が水平な砂層の平面積(表面負荷率)を基準としているが、その砂層を水平でなく「縦配置」にすることにより省スペースにすることが可能になるのであるが、この「縦配置」は生物膜を構成する好気性微生物への酸素の供給という点から従来は困難とされていたのを、本考案は簡単な電気分解装置(電解装置)を付加することにより解決したのである。
すなわち従来は大気と接する「ろ過池」の水面積から微生物に必要な酸素を大気中から取り込んでいるので、「縦配置」にすれば水面積が縮小され、当然のことながら酸素が不足になる。
その解決方法として本考案では、請求項1乃至3の考案に限定されるが、電気分解装置(電解装置)を付加することにしたのである。
次に本考案の第2の目的は、「生物処理による浄化法(浄水処理法)」における重要な問題であった生物膜の維持管理を省力化及び効率化することにある。
この第2の目的達成のために、まず「生物膜」の構造乃至構成を改良した、その詳細は後述する。
次に省力化及び効率化のために、請求項1乃至3の考案に限定されるが、それらの「電解装置」を酸素供給だけでなく塩素供給も可能にし、そしてそれら選択切り替え可能にし、生物膜の維持管理の省力化及び効率化のための主要な役割を「電解装置」に持たせたのである。
さらに省力化及び効率化のために、具体的構成の詳細は後述するが、「生物膜」の構成(該「生物膜」を複数の構成とし、そのひとつ)として「流動する浮遊担体」なるものを用いて、それが流動することによる物理的作用を生物膜の維持管理の省力化及び効率化に用いたのである。
The first object of the present invention is to save space while using the principle of "J Simpson's slow sand filtration method" or "purification method by biological treatment (water purification method)", and the second purpose of the present invention is to save space. The purpose is to save labor in the management of biological membranes, and the third purpose of the present invention is to add a microporous physical microfiltration treatment step as the next step of the filtration pond to ensure the safety of water purification treatment. The purpose is three.
The above three purposes are explained below:
The first object of the present invention is to use the principle of "purification method by biological treatment (water purification method)" and structurally improve it in order to solve the above-mentioned problems of the conventional rapid filtration method. This is to further put into practical use the "purification method by biological treatment (water purification method)".
That is, the improvement point is that in the conventional "purification method by biological treatment (water purification method)", the "filtered water amount" is based on the horizontal area (surface load factor) of the horizontal sand layer, but the sand layer is horizontal. It is possible to save space by using "vertical arrangement" instead, but this "vertical arrangement" has been considered difficult in the past in terms of supplying oxygen to the aerobic microorganisms that make up the biofilm. However, the present invention was solved by adding a simple electrolyzer (electrolyzer).
In other words, conventionally, oxygen required for microorganisms is taken in from the atmosphere from the water area of the "filtration pond" that is in contact with the atmosphere, so if it is "vertically arranged", the water area will be reduced and, of course, oxygen will be insufficient. ..
As a solution to this problem, the present invention is limited to the inventions of claims 1 to 3, but an electrolyzer (electrolyzer) is added.
Next, the second object of the present invention is to save labor and improve the efficiency of maintenance of biofilm, which has been an important problem in the "purification method by biological treatment (water purification method)".
In order to achieve this second purpose, the structure or composition of the "biofilm" was first improved, the details of which will be described later.
Next, for labor saving and efficiency improvement, although limited to the inventions of claims 1 to 3, those "electrolyzers" can supply not only oxygen but also chlorine, and can switch between them, and biofilms. The "electrolyzer" was given the main role of labor saving and efficiency improvement of the maintenance of the film.
Further, in order to save labor and improve efficiency, the details of the specific configuration will be described later, but the configuration of the "biofilm" (the "biofilm" has a plurality of configurations and one of them) is a "flowing floating carrier". Was used to save labor and improve efficiency in the maintenance of biofilms by using the physical action of the flow of the biofilm.

以下各々について説明する。
まず「生物膜(生物ろ過膜)」であるが、これは以下の2つの構成からなり:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された砂等の多様なろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重の多孔質体等の生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の2つで構成される。
前記第2の担体については、その浮遊状態の制御により、前記第1の生物ろ過膜の状態を最適化するために用いることが可能になる。
次に、請求項1乃至3の考案に限定されるが、その「電解装置」について説明すれば、その設置位置は大きく分類して2つの設置位置があり、
まず第1の設置位置は、ろ過池において縦型枠組構造体の間(ある間隔で設置される場合はそれらのゾーンの間)の水中に、該水中の上下方向は任意(例えば底部、中部等)に選択可能に設置される。
次に第2の設置位置は、生物膜によるろ過工程の後であり、かつ次の工程である精密ろ過工程の入り口において、消毒目的の塩素を発生させるために、ここにも電解装置が設置される。
従って、まずろ過池の電解装置について説明し、その後に精密ろ過工程の入り口の電解装置について説明する。
すなわち、ろ過池の電解装置の第1の機能としては、これで生成される酸素ガスを水中に生成溶存させることで微生物の硝化、脱窒、食物連鎖の活性化を図る。
Each will be described below.
The first is "biofilm (biofiltration membrane)", which consists of the following two configurations:
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various filter media layers such as sand stored in the structure (because it is a container). Biofilm composed of microorganisms The second is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place such as a porous body having a specific gravity similar to that of water, and is abundant in the water of a filtration pond. It is composed of the above two that exist in a fluid state.
By controlling the floating state of the second carrier, it becomes possible to use it for optimizing the state of the first biofiltration membrane.
Next, although limited to the inventions of claims 1 to 3, if the "electrolyzer" is described, the installation positions are roughly classified into two installation positions.
First, the first installation position is in the water between the vertical frame structures (between those zones when installed at a certain interval) in the filtration pond, and the vertical direction of the water is arbitrary (for example, bottom, middle, etc.). ) Can be selected.
Next, the second installation position is after the biofilm filtration process, and at the entrance of the microfiltration process, which is the next process, an electrolytic device is also installed here in order to generate chlorine for disinfection purposes. To.
Therefore, the electrolyzer of the filtration pond will be described first, and then the electrolyzer at the entrance of the microfiltration step will be described.
That is, the first function of the electrolytic device of the filtration pond is to nitrify, denitrify, and activate the food chain of microorganisms by generating and dissolving the oxygen gas generated by the electrolytic device in water.

すなわち電解装置は、酸素を発生させて水の溶存酸素濃度を最適制御することにより好気性微生物の活動(主として硝化活動)を促進させる。
逆に電解装置の位置(酸素の発生位置)を上下に変化させることにより酸素不足エリアを作り出し、該酸素不足エリアで嫌気性微生物を活性化させるためにも用いることが可能になる。
ろ過池の電解装置の第2の機能としては、生物膜の維持管理の省力化及び効率化のための機能である。
すなわち電解装置は、塩素を発生させて微生物が付着して形成されているバイオ膜(生物膜)を自動更新するためにも用いられる。
バイオ膜(生物膜)での損失水頭の自動制御と「ろ過池」内部、特に「生物膜」、の定期的消毒及び洗浄の自動化(それにより人力による洗浄周期が延長される)が可能になる。すなわち「生物膜」での損失水頭の自動制御と「ろ過池内部の定期的消毒の自動化」(それにより人力による洗浄周期が延長される)が可能になる。
「生物膜」の洗浄について、詳細は後述するが、次の3つの洗浄がある:
1.水を順方向に流しながら洗浄する(以下「順洗浄」という)。
2.水を逆方向に流しながら洗浄する(以下「逆洗浄」という)。
3.「生物膜」を構成する「容器状の縦型枠組構造体」の表面を洗浄する(以下「表面洗浄」という)。
以上の3つの洗浄の詳細は後述する(図面に示して説明する)。
また「ろ過池内部の定期的消毒及び洗浄」は、「ろ過池」を複数設けておき、それらの「ろ過池」を順次休止し(特定のものを休止し)洗浄する方法を用いるべきであり、それにより定期的消毒及び洗浄を現実的に行うことが可能になる。
That is, the electrolyzer promotes the activity of aerobic microorganisms (mainly nitrification activity) by generating oxygen and optimally controlling the dissolved oxygen concentration of water.
On the contrary, by changing the position of the electrolyzer (the position where oxygen is generated) up and down, an oxygen deficient area can be created, and it can be used to activate anaerobic microorganisms in the oxygen deficient area.
The second function of the electrolytic device of the filtration pond is a function for labor saving and efficiency improvement of maintenance of the biofilm.
That is, the electrolyzer is also used to automatically renew the biofilm (biofilm) formed by generating chlorine and adhering microorganisms.
Enables automatic control of head loss in biofilms and automation of periodic disinfection and cleaning of the interior of the "filtration pond", especially the "biofilm" (which extends the manual cleaning cycle). .. That is, it is possible to automatically control the head loss in the "biofilm" and "automate the periodic disinfection inside the filtration pond" (which extends the manual cleaning cycle).
The details of cleaning the "biofilm" will be described later, but there are three types of cleaning:
1. 1. Wash while flowing water in the forward direction (hereinafter referred to as "forward washing").
2. 2. Wash while flowing water in the opposite direction (hereinafter referred to as "backwash").
3. 3. The surface of the "container-shaped vertical frame structure" that constitutes the "biofilm" is cleaned (hereinafter referred to as "surface cleaning").
Details of the above three cleanings will be described later (described in the drawings).
In addition, for "regular disinfection and cleaning inside the filtration pond", a method should be used in which multiple "filtration ponds" are provided and those "filtration ponds" are sequentially paused (specific ones are paused) for cleaning. , It makes it possible to carry out regular disinfection and cleaning realistically.

次に精密ろ過工程の入り口の電解装置の機能とは、前記ろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し、該微細多孔の物理的精密ろ過処理工程の入り口において、消毒目的の塩素を発生させるために設ける電解装置についての機能である。
生物膜によるろ過工程の後であり、かつ次の工程(終段工程)である微細多孔の物理的精密ろ過処理工程の入り口において、消毒目的の塩素を発生させるために新たな電解装置が設けられる。
すなわち消毒目的の塩素についてこの電解装置で発生させた塩素を用いるのである。
なお付言すれば電解装置による塩素発生技術は一例として特開2004−143481、特許2711382、特許3357008等に公知である。
電解装置において微量の食塩水を電解室内に添加すれば、食塩水の電解となり塩素が発生する。
Next, the function of the electrolyzer at the entrance of the precision filtration step is to add a microporous physical precision filtration treatment step as the next step of the filtration pond, and at the entrance of the microporous physical precision filtration treatment step. This is a function of an electrolytic device provided to generate chlorine for disinfection purposes.
A new electrolyzer will be installed to generate chlorine for disinfection purposes at the entrance of the microporous physical microfiltration process, which is the next step (final step) after the biological membrane filtration step. ..
That is, chlorine generated by this electrolyzer is used for chlorine for disinfection purposes.
In addition, the chlorine generation technique by the electrolytic device is known as an example in Japanese Patent Application Laid-Open No. 2004-143481, Japanese Patent 2711382, Japanese Patent 3357008 and the like.
If a small amount of saline solution is added to the electrolysis chamber in the electrolyzer, the saline solution is electrolyzed and chlorine is generated.

本考案の第2の目的は前述の通り、「生物処理による浄化法(浄水処理法)」における重要な問題であった生物膜の維持管理を省力化及び効率化することにあったが、それに関して生物膜の構成と電解装置について説明した。
ここで電解装置はあくまでも酸素供給手段または洗浄手段のひとつであるから、酸素供給手段についてはポンプによる散水、水中キャビテーション、(空気の)マイクロバブリングで置換してもよく、また洗浄手段については塩素を電解装置によることなく直接塩素注入してもよく、さらに塩素による洗浄でなく縦型枠組構造体や物理的精密ろ過装置を超音波洗浄で洗浄してもよい。
次に本考案の第3の目的であるが、前記ろ過池の次の工程として微細多孔の物理的精密ろ過工程を付加することにある。
すなわち前記生物膜によるろ過工程の次の工程として、微細多孔の物理的精密ろ過、例えば縦型陶板(例えばNF/2mm級)によるろ過、あるいは物理処理を目的とした砂ろ過(これもスペース的にも、また洗浄のためにも縦型が望ましい)、による「ろ過」(以下「微細多孔の物理的精密ろ過」と称する)を行ない、生物膜による「ろ過」を補完することにある。
この「微細多孔の物理的精密ろ過」は前段の生物膜によるろ過工程でブレークスルー等のアクシデントが発生した場合に「ろ過水(浄水)」の安定性を確保するものである。
この「微細多孔の物理的精密ろ過」は常圧(ポンプ等で加圧して「ろ過」するのでなく水面の水頭の圧力で「ろ過」するという意味である)で行われ、前述の通り生物膜によるろ過工程の次の工程(言い換えれば最終工程)であるから既に生物膜で浄化されており、その結果ろ過面の汚染は限定的であり、電解塩素の作用でその洗浄の必要性はほとんどない。
次に「生物膜(生物ろ過膜)」の他の構成を次に説明する:
すなわち「生物膜(生物ろ過膜)」として、
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された砂等の多様なろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重の多孔質体等の生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の2つで構成される「生物膜(生物ろ過膜)」を説明した。
しかし「生物膜(生物ろ過膜)」を他の構成にすることも可能であり、それを次に説明する:
すなわち縦型枠組構造体は同様な位置に設けるが、該縦型枠組構造体には砂等のろ材層を収納しない、すなわち何も収納しない、いわば「空の枠組構造体」、すなわち枠組構造体自体が「ろ過板」であって、一重乃至多重の「ろ過板」にし、この「ろ過板」に水が接触して流れるのでありその際に生物居所となっている「ろ過板」(その表面や多孔板の場合にはその孔)に生物が生息して「生物膜(生物ろ過膜)」として機能する。
As described above, the second purpose of the present invention was to save labor and improve the efficiency of maintenance of biofilm, which was an important problem in the "purification method by biological treatment (water purification method)". The composition of the biofilm and the electrolyzer were explained.
Here, since the electrolyzer is only one of the oxygen supply means or the cleaning means, the oxygen supply means may be replaced by watering with a pump, underwater cavitation, or micro bubbling (of air), and chlorine may be used for the cleaning means. Chlorine may be directly injected without using an electrolyzer, and the vertical frame structure or the physical precision filtration device may be cleaned by ultrasonic cleaning instead of cleaning with chlorine.
Next, a third object of the present invention is to add a microporous physical microfiltration step as a next step of the filtration pond.
That is, as the next step of the filtration step using the biological membrane, microporous physical microfiltration, for example, filtration by a vertical ceramic plate (for example, NF / 2 mm class), or sand filtration for the purpose of physical treatment (also in terms of space). Also, vertical type is desirable for cleaning), and "filtration" (hereinafter referred to as "microporous physical microfiltration") is performed to complement "filtration" by biological membrane.
This "microporous physical microfiltration" ensures the stability of "filtered water (purified water)" when an accident such as breakthrough occurs in the filtration process using the biofilm in the previous stage.
This "microporous physical microfiltration" is performed at normal pressure (meaning that "filtration" is performed by the pressure of the head of the water surface instead of "filtering" by pressurizing with a pump or the like), and as described above, the biological membrane. Since it is the next step (in other words, the final step) of the filtration process, it has already been purified by the biomembrane, and as a result, the contamination of the filtration surface is limited, and there is almost no need for cleaning due to the action of electrolytic chlorine. ..
Next, other configurations of "biofilm (biofiltration membrane)" will be described below:
That is, as a "biofilm (biofiltration membrane)"
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various filter media layers such as sand stored in the structure (because it is a container). Biofilm composed of microorganisms The second is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place such as a porous body having a specific gravity similar to that of water, and is abundant in the water of a filtration pond. The "biofilm (biofiltration membrane)" composed of the above two substances that exist in a fluid state has been described.
However, it is possible to make the "biofilm (biofiltration membrane)" into other configurations, which will be explained below:
That is, the vertical frame structure is provided at the same position, but the vertical frame structure does not store a filter medium layer such as sand, that is, does not store anything, so to speak, an "empty frame structure", that is, a frame structure. It is a "filter plate" itself, and it is made into a single or multiple "filter plate", and water comes into contact with this "filter plate" and flows, and at that time, the "filter plate" (its surface) is the place of life. In the case of a perforated plate or a perforated plate, organisms inhabit the pores) and function as a "biological membrane (biological filtration membrane)".

本考案は以上の目的達成のために:
請求項1として、濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設けた、以上の浄水処理装置を提案するものである。
請求項2として、濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設けた、以上の浄水処理装置を提案するものである。
請求項3として、濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設け、前記ろ過池の次の工程として微細多孔の物理的精密ろ過工程を付加し、次に前記生物膜によるろ過工程の後であり、かつ前記微細多孔の物理的精密ろ過工程の入り口において、消毒目的の塩素を発生させる電解装置を設けた、以上の浄水処理装
を提案するものである。
さらに本考案は請求項4乃至8の浄水処理装置及び関連考案としての電解装置(記載を省略する、実用新案登録請求の範囲を参照下さい)を提案するものである。
The present invention aims to achieve the above objectives:
Claim 1 is a water purification device that purifies treated water that has been treated to reduce turbidity or raw water with a turbidity concentration of 10 mg / l or less, and is a biological film provided in a filtration pond, the organism. What is a membrane:
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biofilm, which is composed of microorganisms inhabiting the filter medium layer, has a specific gravity similar to that of water and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place formed of a porous body, and is a first and second biofilm that is present in a large number of fluid states in the water of a filtration pond. The treated water or the raw water having a turbidity concentration of 10 mg / l or less was brought into contact with the water, and then an electrolysis device (electrolytic device) was provided in the water of the filtration pond so that the vertical direction of the water could be arbitrarily selected. , The above water purification equipment is proposed.
Claim 2 is a water purification apparatus for purifying treated water treated to reduce turbidity or raw water having a turbidity concentration of 10 mg / l or less, and a biological film provided in a filtration pond, the organism. What is a membrane:
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biofilm, which is composed of microorganisms inhabiting the filter medium layer, has a specific gravity similar to that of water and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place formed of a porous body, and is a first and second biofilm that is present in a large number of fluid states in the water of a filtration pond. The treated water or the raw water having a turbidity concentration of 10 mg / l or less was brought into contact with the water, and then an electrolysis device (electrolytic device) was provided in the water of the filtration pond so that the vertical direction of the water could be arbitrarily selected. , The above water purification equipment is proposed.
Claim 3 is a water purification device that purifies treated water that has been treated to reduce turbidity or raw water with a turbidity concentration of 10 mg / l or less, and is a biological film provided in a filtration pond, the organism. What is a membrane:
The first is a biological membrane formed by inhabiting microorganisms on the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biological membrane composed of microorganisms inhabiting the filter medium layer has a specific gravity similar to that of water, and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biological membrane composed of microorganisms inhabiting a carrier that serves as a biological residence formed of a porous body, and is a first and second biological membrane that is present in a large number of fluid states in the water of a filtration pond. The treated water or the raw water having a turbidity concentration of 10 mg / l or less is brought into contact with the water, and then an electrolysis device (electrolytic device) is provided in the water of the filtration pond so that the vertical direction of the water can be arbitrarily selected. A microporous physical precision filtration step is added as the next step of the filtration pond, and then after the microporous physical precision filtration step and at the entrance of the microporous physical precision filtration step, for disinfection purposes. We propose the above water purification treatment equipment equipped with an electrolytic device that generates chlorine.
Further, the present invention proposes the water purification apparatus according to claims 4 to 8 and the electrolytic apparatus as a related invention (the description is omitted, refer to the scope of claims for utility model registration).

本考案の浄水処理装置の効果を次に列挙する。
1.本考案の浄水処理装置は、容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜を用いるため、すなわち「縦型」であるため、省スペースが図れる。
例えば縦型枠組構造体は従来の同機能の設備と比較して1/30程度のスペースにすることが可能であるから既設の沈殿池に設置可能である。
2.本考案の浄水処理装置は、電気分解装置(電解装置)を設けた場合には(請求項1乃至3の場合には)生物膜に十分な酸素を供給できるだけでなく、生物膜の維持管理の省力化及び効率化も可能になった。
3.本考案の浄水処理装置は、生物膜のろ過工程の次に微細多孔の物理的精密ろ過処理工程を付加した場合には(請求項2乃至3の場合には)、生物膜のろ過工程でのブレークスルーが生じた場合等の安全対策になる。
4.本考案の浄水処理装置は、生物膜のろ過工程の次の微細多孔の物理的精密ろ過処理工程の入り口において、消毒目的の塩素を発生させる電解装置を設けた場合には(請求項3の場合には)、物理的精密ろ過のために設けられた微細孔の閉塞を防止し、ろ過継続時間を長くするだけでなく、該工程を経由した水に0.3mg/l程度の残留塩素濃度(水道水として付与しなければならない)を与えることが可能になる。
前記0.3mg/l程度の残留塩素濃度について付言すれば、給水栓水0.1mg/lにするには従来の急速ろ過法での塩素注入率のトータルが10mg/lにもなる場合もあったのと比較して圧倒的に塩素注入量を低減することが可能になっている(特にアジア地域の浄水処理に適する)。
The effects of the water purification apparatus of the present invention are listed below.
1. 1. The water purification apparatus of the present invention has a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various simple units housed in the structure (because it is a container). Space can be saved because a biofilm composed of microorganisms inhabiting a filter medium layer provided in a layer or multiple layers is used, that is, because it is "vertical".
For example, the vertical frame structure can be installed in an existing settling basin because the space can be reduced to about 1/30 of that of the conventional equipment having the same function.
2. 2. The water purification device of the present invention can not only supply sufficient oxygen to the biofilm (in the case of claims 1 to 3) when an electrolyzer (electrolyzer) is provided, but also maintain the biofilm. Labor saving and efficiency improvement have also become possible.
3. 3. In the water purification apparatus of the present invention, when a microporous physical microfiltration treatment step is added after the biological membrane filtration step (in the case of claims 2 to 3), the biological membrane filtration step is performed. It is a safety measure in case of breakthrough.
4. In the case of the water purification apparatus of the present invention, when an electrolytic device for generating chlorine for disinfection is provided at the entrance of the microporous physical microfiltration treatment step following the biological membrane filtration step (in the case of claim 3). In addition to preventing the blockage of micropores provided for physical microfiltration and prolonging the filtration duration, the residual chlorine concentration of about 0.3 mg / l in the water that has passed through the process ( Must be given as tap water) can be given.
In addition to the residual chlorine concentration of about 0.3 mg / l, the total chlorine injection rate in the conventional rapid filtration method may be as high as 10 mg / l in order to make the faucet water 0.1 mg / l. It is possible to reduce the amount of chlorine injection overwhelmingly compared to the above (especially suitable for water purification treatment in the Asian region).

本考案の実施形態に係る浄水処理装置のフロー図である。It is a flow chart of the water purification apparatus which concerns on embodiment of this invention. 本考案の実施形態に係る浄水処理装置の概念図である。It is a conceptual diagram of the water purification apparatus which concerns on embodiment of this invention. 本考案の実施形態に係る浄水処理装置のろ過運転時の概念図である。It is a conceptual diagram at the time of the filtration operation of the water purification apparatus which concerns on embodiment of this invention. 本考案の実施形態に係る浄水処理装置の洗浄運転時の概念図である。It is a conceptual diagram at the time of cleaning operation of the water purification apparatus which concerns on embodiment of this invention. 本考案の実施形態に係る浄水処理装置の表面洗浄運転時の概念図である。It is a conceptual diagram at the time of the surface cleaning operation of the water purification apparatus which concerns on embodiment of this invention. 本考案の実施形態に係る浄水処理装置の逆流洗浄運転時の概念図である。It is a conceptual diagram at the time of the backflow washing operation of the water purification apparatus which concerns on embodiment of this invention.

以下本考案の浄水処理装置を図面に示す実施例に従って説明する。
図1は前段工程(90)と本考案の浄水処理装置(2)を有する浄水工程(1)のフロー図を示し、該浄水処理装置(2)の詳細は図2に示される。
すなわち図2を参照して、本考案はフロック等を沈殿させた沈殿処理水または濁度が低い原水では沈殿処理不要の原水の浄水処理を行うものであるが、まずフロック等を沈殿させる工程は従来公知であるから簡単に説明する。
但しこのフロック等の沈殿工程は沈殿池Fで行われ、原水の濁質濃度10mg/l以下の(汚濁が低い)場合には省略可能である。
すなわち沈殿池Fに設置された沈殿装置は前工程で注入された凝集剤により形成されたフロック等を沈殿させ、すなわち沈殿除去するものである。
前記沈殿池Fでフロック等を沈殿乃至沈降させた後の上澄水を浄化するのが本考案であり、以下本考案の浄水処理装置(2)を説明する。
すなわち図2に示す様に、ろ過池(Gの池)が前記沈殿池Fにプロセス的に接続されて設けられ、本考案の浄水処理装置(2)を構成する生物ろ過処理工程Gは該ろ過池に設けられる。
すなわち図示の浄水処理装置(2)の生物ろ過処理工程Gは「生物処理による浄化法」としての常圧式縦型生物ろ過装置であり、該ろ過池内に設けられる。
該常圧式縦型生物ろ過装置は「生物膜」を有し、該生物膜とは:第1は容器状の縦型枠組構造体と該構造体内(容器になっているから容器内)に収納された砂等の多様な単層または複層設けられたろ材層第2は水と同程度の比重の多孔質体等の生物居所となる担体であり、ろ過池の水中に多数流動状態で複数の前記縦型枠組構造体の相互の間に存在させるもの以上の2つで構成される。
Hereinafter, the water purification apparatus of the present invention will be described with reference to Examples shown in the drawings.
FIG. 1 shows a flow chart of a water purification process (1) having a pre-stage step (90) and the water purification apparatus (2) of the present invention, and details of the water purification apparatus (2) are shown in FIG.
That is, with reference to FIG. 2, the present invention purifies the raw water that does not require precipitation treatment with the precipitated treated water in which flocs and the like are precipitated or the raw water having low turbidity. Since it is known in the past, it will be briefly described.
However, this settling step for flocs and the like is performed in the settling basin F, and can be omitted when the turbidity concentration of the raw water is 10 mg / l or less (low pollution).
That is, the settling device installed in the settling basin F precipitates, that is, removes the flocs and the like formed by the flocculant injected in the previous step.
It is the present invention to purify the supernatant water after the flocs and the like are settled or settled in the settling basin F, and the water purification apparatus (2) of the present invention will be described below.
That is, as shown in FIG. 2, a filtration pond (G pond) is provided by being processally connected to the settling basin F, and the biological filtration treatment step G constituting the water purification apparatus (2) of the present invention is the filtration. It is installed in the pond.
That is, the biological filtration treatment step G of the water purification device (2) shown in the figure is a normal pressure type vertical biological filtration device as a "purification method by biological treatment", and is provided in the filtration pond.
The atmospheric pressure type vertical biofiltration device has a "biological membrane", and the biological membrane is: the first is a container-shaped vertical frame structure and the inside of the structure (because it is a container, it is stored in the container). The second filter medium layer, which is provided with various single layers or multiple layers such as sand, is a carrier that serves as a living place for a porous body having a specific gravity similar to that of water, and is present in a large number of fluid states in the water of the filtration pond. It is composed of the above two that exist between the vertical frame structures of the above.

まず第1は、1mm〜2mm厚さ等の多孔質材、メッシュ材等のろ材を収容可能な強度を有し、水が通過可能にされた、各種構造板、具体例を例示すれば多数の網目、細かい孔等を有して水が通過可能なチタン等の板で容器状に作られた縦型枠組構造体が設けられる。該構造体内(容器になっているから容器内)に収納された砂(前記多孔質の孔、網目、細かい孔等を通過しない程度の粒の大きさ)の砂層を有する。
縦型枠組構造体の両側外面及び砂層の内部には微生物が生息して「生物膜」(「砂内部」の生物を含めて以下「生物膜」と称する)が構成されることになる。
ここで「生物膜」なる用語は砂内部の生物を含む概念であり、また縦型枠組構造体の両側外面、砂層の内部、砂内部、なる用語における「砂」とは「砂等の多様な単層または複層設けられたろ材層」を含む概念である。
次に「生物膜」の第2は水と同程度の比重の多孔質体等の生物居所となる担体であり、ろ過池の水中に多数流動状態で複数の前記縦型枠組構造体の相互の間に存在させるものである。
すなわち水と同程度の比重の多孔質体等の生物居所となる担体(例えば活性炭の粒であり、該粒の大きさは前記縦型枠組構造体の多孔質の孔、網目または細かい孔を通過しない程度の大きさ)であり、ろ過池の水中に多数流動状態で複数の前記縦型枠組構造体の相互の間に存在させるものである。
以上の第2の担体にも自然の原水に含まれる微生物が生息して「生物膜」が構成される。また「縦型」の意味であるが、容器状の枠組構造体がろ過池に縦方向に(池の上下方向に)設置される意味である。
枠組構造体の多孔質の孔、網目または細かい孔を外側から内側へと、さらに砂層を上から下へと常圧で(すなわちポンプ等で加圧することなく水頭差の圧力で)水が流入ろ過されていき、その過程で水は縦型枠組構造体の両側外面及び砂層の内部の微生物の「生物膜」(「砂内部」の生物を含めて「生物膜」と称する)と接触して浄化される(砂層での物理的ろ過を含む意味である)。
First, various structural plates having a strength capable of accommodating a porous material having a thickness of 1 mm to 2 mm and a filter material such as a mesh material and allowing water to pass through, and a large number of specific examples. A vertical frame structure made in a container shape with a plate such as titanium having a mesh, fine holes, etc. and allowing water to pass through is provided. It has a sand layer of sand (grain size that does not pass through the porous pores, mesh, fine pores, etc.) stored in the structure (because it is a container, so that it is inside the container).
Microorganisms inhabit the outer surfaces on both sides of the vertical frame structure and the inside of the sand layer to form a "biofilm" (hereinafter referred to as "biofilm" including organisms "inside the sand").
Here, the term "biological film" is a concept that includes organisms inside sand, and "sand" in the term "sand" is "various types such as sand" on both outer surfaces of a vertical frame structure, inside a sand layer, and inside sand. It is a concept including "a filter medium layer provided with a single layer or multiple layers".
Next, the second "biofilm" is a carrier that serves as a living place for a porous body or the like having a specific gravity similar to that of water, and a large number of the above-mentioned vertical framework structures are in a state of mutual flow in the water of a filtration pond. It is something that exists in between.
That is, a carrier that serves as a living place for a porous body having a specific gravity similar to that of water (for example, grains of activated carbon, and the size of the grains passes through the porous pores, mesh, or fine pores of the vertical framework structure. It is a size that does not occur), and is present in a large number of flowing states in the water of the filtration pond between the plurality of vertical framework structures.
Microorganisms contained in natural raw water also inhabit the above-mentioned second carrier to form a "biofilm". Further, the meaning of "vertical type" means that the container-shaped frame structure is installed in the filtration pond in the vertical direction (vertical direction of the pond).
Porous pores, meshes or fine holes in the framework structure are filtered from the outside to the inside, and the sand layer is filtered from the top to the bottom at normal pressure (that is, at the pressure of the head difference without pressurizing with a pump or the like). In the process, water is purified by contacting with the "biological membrane" of microorganisms on both outer surfaces of the vertical framework structure and inside the sand layer (including the organisms "inside the sand", it is called "biological membrane"). (Meaning to include physical filtration in the sand layer).

また砂層は物理的ろ過作用(例えばクリプト原虫等を補足して通過させない)もあるが、前記生物浄化作用が主たるものである。
前記第2の担体は水と同程度の比重でろ過池の水中に電解装置により発生した酸素気泡により多数流動状態で存在させたものであるから、ろ過池内の前記第1の容器状の縦型枠組構造体の両側外面に水の流れと共に接触することになり該構造体の外面の生物膜の表面を擦って削る作用を有し、従って生物膜の膜厚が厚くなり過ぎることを物理的に防止している。
この縦型枠組構造体は、ろ過池内に着脱自在に、また多段、多行、多列に複数設置して、それらを必要に応じて相互に直列に連結、及び/または並列に連結してもよい。
またろ過池自体も、図2に示す様に相互に遮断可能に並列に複数設けることにより、あるろ過池は使用中にし、同時に他のあるろ過池は生物膜の保守や洗浄(逆流によるろ層深部の洗浄と表面表層部の洗浄)中にし、という様に浄水場全体の運転システムを考慮した(すなわちノンストップ運転を考慮した)設置にしなければならない。
The sand layer also has a physical filtration action (for example, it does not allow cryptoprotozoans and the like to pass through), but the biological purification action is the main one.
Since the second carrier has a specific gravity similar to that of water and is allowed to exist in a large number of fluid states in the water of the filtration pond due to oxygen bubbles generated by the electrolytic device, the first container-shaped vertical type in the filtration pond. It comes into contact with the outer surfaces on both sides of the frame structure together with the flow of water, and has the effect of rubbing and scraping the surface of the biological film on the outer surface of the structure, thus physically preventing the biological film from becoming too thick. It is preventing.
This vertical frame structure can be detachably installed in the filtration pond, and can be installed in multiple stages, multiple rows, and multiple columns, and they can be connected in series and / or in parallel as needed. Good.
In addition, as shown in FIG. 2, a plurality of filtration ponds themselves are provided in parallel so as to be able to block each other so that one of the filtration ponds is in use and at the same time, another filter pond is used for maintenance and cleaning of biological membranes (filter layer due to backflow). It must be installed in consideration of the operation system of the entire water purification plant (that is, in consideration of non-stop operation), such as during deep cleaning and surface surface cleaning).

都市部の浄水の原水は大水量で汚濁している場合が多いが、この様な原水では本考案の縦型枠組構造体に砂を収納した縦型枠組構造体は特に省スペースに寄与する。
また縦型であるから、例えば構造体の両外面を「生物膜」にすることで構造体内に収納する砂等の「多様なろ材」の量を節約できる。
また「多様なろ材」の材質として石英、ガーネット、トルマリン、黒曜石、柘榴石、パーライト、真珠石、無煙炭(アンスラサイト)、珪砂、活性炭、焼結アルミナ等を合理的に選択可能である。
次に「電解装置」については「考案が解決しようとする課題」の欄で詳細にその機能を分類して既に説明したが、重複する部分もあるが、以下に再度説明しておく。
すなわち「電解装置」の設置位置は大きく分類して2つの設置位置があり、図3に示す様にまず第1の設置位置として電解装置(6)は、生物ろ過処理工程Gのろ過池において縦型枠組構造体(3)の間(図示の様にゾーンで設置される場合はそれらのゾーンの間)の水中に、該水中の上下方向は任意(例えば底部、中部等)に選択可能に設置される。
次に第2の設置位置は、図3に示す様に生物ろ過処理工程G(生物膜によるろ過工程)の後であり、かつ次の工程である物理的精密ろ過装置(10)による精密ろ過工程の入り口において、消毒目的の塩素を発生させるために新たな電解装置(8)が設置される。
従って、まずろ過池の電解装置(6)について説明し、その後に物理的精密ろ過装置(10)による精密ろ過工程の入り口の電解装置(8)について説明する。
The raw water of purified water in urban areas is often polluted with a large amount of water, but in such raw water, the vertical frame structure in which sand is stored in the vertical frame structure of the present invention particularly contributes to space saving.
Further, since it is a vertical type, for example, by making both outer surfaces of the structure into "biofilms", the amount of "various filter media" such as sand stored in the structure can be saved.
Quartz, garnet, tourmaline, obsidian, garnet, pearlite, pearl stone, smokeless charcoal (anthracite), silica sand, activated charcoal, sintered alumina, etc. can be reasonably selected as the material of "various filter media".
Next, the "electrolyzer" has already been described by classifying its functions in detail in the column of "problems to be solved by the device", but there are some overlaps, but it will be explained again below.
That is, the installation positions of the "electrolyzer" are roughly classified into two installation positions. As shown in FIG. 3, the electrolyzer (6) is vertically installed in the filtration pond in the biological filtration process G as the first installation position. Installed in water between the frame structures (3) (between those zones when installed in zones as shown), and in the vertical direction of the water can be selected arbitrarily (for example, bottom, middle, etc.). Will be done.
Next, the second installation position is after the biological filtration treatment step G (filtration step by biological membrane) as shown in FIG. 3, and the next step is the precision filtration step by the physical microfiltration device (10). A new electrolyzer (8) is installed at the entrance to generate chlorine for disinfection purposes.
Therefore, the electrolyzer (6) of the filtration pond will be described first, and then the electrolyzer (8) at the entrance of the microfiltration step by the physical microfiltration device (10) will be described.

すなわち、ろ過池の電解装置(6)の第1の機能としては、これで生成される酸素ガスを水中に生成溶存させることで微生物の硝化、脱窒(脱チッソ)、食物連鎖の活性化を図る。
すなわち電解装置(6)は、酸素を発生させて水の溶存酸素濃度を上げることにより好気性微生物の活動(主として硝化活動)を促進させる。
逆に電解装置(6)の位置(酸素の発生位置)を上下に変化させることにより酸素不足エリアを作り出し、該酸素不足エリアで嫌気性微生物を活性化させるため(主として脱チッソさせるため)にも用いることが可能になる。
ここで電解装置(6)はあくまでも酸素供給手段または洗浄手段のひとつであるから、酸素供給手段についてはポンプによる散水、水中キャビテーション、(空気の)マイクロバブリングで置換してもよい。
また「生物膜」の膜厚の制御だけに注目すれば、電解装置(6)以外にエアーノズル等を用いて膜厚を物理的に制御する(薄い膜厚にすることを含む)ことも可能である。
ろ過池の電解装置(6)の第2の機能としては、生物膜の維持管理の省力化及び効率化のための機能である。
すなわち電解装置(6)は、モードが切り替えられて、塩素を発生させて縦型枠組構造体(3)等の微生物が付着して形成されているバイオ膜(生物膜)を自動更新するためにも用いられる。
バイオ膜(生物膜)での損失水頭の自動制御とろ過池内部の定期的消毒及び洗浄の自動化(それにより人力による洗浄周期が延長される)が可能になる。
That is, the first function of the electrolytic device (6) of the filtration pond is to nitrify, denitrify (denitrify) microorganisms, and activate the food chain by generating and dissolving the oxygen gas generated by this in water. Try.
That is, the electrolyzer (6) promotes the activity of aerobic microorganisms (mainly nitrification activity) by generating oxygen to increase the dissolved oxygen concentration of water.
Conversely, by changing the position of the electrolyzer (6) (oxygen generation position) up and down, an oxygen-deficient area is created, and in order to activate anaerobic microorganisms in the oxygen-deficient area (mainly to de-chisso). It becomes possible to use.
Here, since the electrolyzer (6) is merely one of the oxygen supply means or the cleaning means, the oxygen supply means may be replaced by watering by a pump, underwater cavitation, or micro bubbling (of air).
Further, if attention is paid only to the control of the film thickness of the "biofilm", it is possible to physically control the film thickness (including making the film thickness thinner) by using an air nozzle or the like in addition to the electrolytic device (6). Is.
The second function of the electrolytic device (6) of the filtration pond is a function for labor saving and efficiency improvement of maintenance of the biofilm.
That is, the electrolyzer (6) is switched in mode to generate chlorine and automatically renew the biofilm (biofilm) formed by attaching microorganisms such as the vertical frame structure (3). Is also used.
It enables automatic control of head loss in biofilms and automation of periodic disinfection and cleaning inside filtration ponds (which extends the manual cleaning cycle).

すなわち縦型枠組構造体(3)等のバイオ膜(生物膜)での損失水頭の自動制御と「ろ過池内部の定期的消毒の自動化」(それにより人力による洗浄周期が延長される)が可能になる。
すなわち「ろ過池内部の定期的消毒の自動化」とは、図2に示す様に複数あるろ過池において、それらのいずれかを順次休止し(特定のものを休止し)洗浄中にすることで縦型枠組構造体(3)等の生物膜の維持管理の省力化及び効率化が図れる。
次に図3に示す物理的精密ろ過装置(10)による精密ろ過工程の入り口の電解装置(8)の機能とは、前記生物ろ過処理工程Gのろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し、該微細多孔の物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させるために設ける電解装置(8)についての機能である。
生物ろ過処理工程Gの生物膜によるろ過工程の後であり、かつ次の工程(終段工程)である微細多孔の物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させるために新たな電解装置(8)が設けられる。
すなわち消毒目的の塩素についてこの電解装置(8)で発生させた塩素を用いるのである。
なお付言すれば電解装置による塩素発生技術は一例として特開2004−143481、特許2711382、特許3357008等に公知である。
電解装置(8)において微量の食塩水を電解室内に添加すれば、食塩水の電解となり塩素が発生する。
また洗浄手段については塩素を電解装置(8)によることなく直接塩素注入してもよく、さらに塩素による洗浄でなく超音波洗浄で洗浄してもよい。
That is, it is possible to automatically control the head loss in the biofilm (biofilm) such as the vertical frame structure (3) and "automate the periodic disinfection inside the filtration pond" (thus extending the manual cleaning cycle). become.
That is, "automation of periodic disinfection inside the filtration pond" means that in a plurality of filtration ponds as shown in FIG. 2, one of them is sequentially paused (a specific one is paused) during cleaning. Labor saving and efficiency of maintenance of biofilms such as the mold structure (3) can be achieved.
Next, the function of the electrolyzer (8) at the entrance of the precision filtration step by the physical precision filtration device (10) shown in FIG. 3 is the physical microporous physical as the next step of the filtration pond in the biological filtration treatment step G. This is a function of the electrolyzer (8) provided for generating chlorine for disinfection purposes at the entrance of the microporous physical precision filtration process H by adding a precision filtration process.
In order to generate chlorine for disinfection purposes at the entrance of the microporous physical microfiltration process H, which is the next step (final step) after the biological filtration step of the biological filtration process G. A new electrolyzer (8) is provided.
That is, chlorine generated by this electrolyzer (8) is used for chlorine for disinfection purposes.
In addition, the chlorine generation technique by the electrolytic device is known as an example in Japanese Patent Application Laid-Open No. 2004-143481, Japanese Patent 2711382, Japanese Patent 3357008 and the like.
If a small amount of saline solution is added to the electrolysis chamber in the electrolyzer (8), the saline solution is electrolyzed and chlorine is generated.
As for the cleaning means, chlorine may be directly injected without using the electrolytic device (8), and further, cleaning may be performed by ultrasonic cleaning instead of cleaning with chlorine.

次に精密ろ過工程の入り口の電解装置(8)の機能とは、前記生物ろ過処理工程Gのろ過池の次の工程として微細多孔の物理的精密ろ過処理工程Hを付加し、物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させるために設ける電解装置(8)についての機能である。
生物ろ過処理工程Gの後であり、かつ次の物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させるために新たな電解装置(8)が設けられる。
すなわち消毒目的の塩素についてこの電解装置(8)で発生させた塩素を用いるのである。
なお付言すれば電解装置による塩素発生技術は一例として特開2004−143481、特許2711382、特許3357008等に公知である。
電解装置(8)において微量の食塩水を電解室内に添加すれば、食塩水の電解となり塩素が発生する。
但し電解装置(8)の代用として電解装置によることなく直接塩素注入してもよく、さらに塩素による洗浄でなく物理的精密ろ過装置(10)を超音波洗浄で洗浄してもよい。
Next, the function of the electrolyzer (8) at the entrance of the precision filtration step is to add a finely porous physical precision filtration treatment step H as a next step of the filtration pond of the biological filtration treatment step G to perform physical precision filtration. This is a function of the electrolytic device (8) provided to generate chlorine for disinfection at the entrance of the treatment step H.
A new electrolyzer (8) is provided after the biofiltration step G and at the entrance of the next physical microfiltration step H to generate chlorine for disinfection purposes.
That is, chlorine generated by this electrolyzer (8) is used for chlorine for disinfection purposes.
In addition, the chlorine generation technique by the electrolytic device is known as an example in Japanese Patent Application Laid-Open No. 2004-143481, Japanese Patent 2711382, Japanese Patent 3357008 and the like.
If a small amount of saline solution is added to the electrolysis chamber in the electrolyzer (8), the saline solution is electrolyzed and chlorine is generated.
However, as a substitute for the electrolyzer (8), chlorine may be directly injected without using the electrolyzer, and the physical microfiltration device (10) may be cleaned by ultrasonic cleaning instead of cleaning with chlorine.

本考案の浄水処理装置の理論を以下に説明する。
すなわち「生物処理による浄化法(浄水処理法)」は捕食、硝化(2NH +3O→2NO +2HO+4H、2NO+O→2NO )、脱窒(通性菌等で硝酸や亜硝酸を分解し除去)、破砕、変成化、吸着といった多様な機能を含む。
好気性微生物依存の硝化により、対象水に溶存するアンモニア態窒素(NH、NHN)を硝化過程で窒素ガス(N)化し、水中から除去することで塩素注入率の低減が可能になる。
また必要な場合には、通性嫌気性微生物に依存する脱窒も可能である。
電解装置は水没形の無隔膜式電解部あるいは隔膜式電解部を選択的に装備すればよく、陽極から酸素ガスを、陰極から水素ガスを通過水中で生成させる。
つまり電解装置はそこにある対象水を原料に電気分解で酸素ガスと水素ガスが必要時に必要量微細気泡で瞬時に対象水に供給できる。
電解部は多段分散、着脱自由に装備可能とし嫌気環境と好気環境をエリア内に形成する。これは従来からの固液分離、脱色、酸化、脱臭等を目的としたいわゆる電解浮上法とは異なり、本考案における電解装置は嫌気性と好気性の環境を提供する手段である。
The theory of the water purification apparatus of the present invention will be described below.
Or "biological treatment purification method with (water purification treatment method)" is predation, nitrification (2NH 4 + + 3O 2 → 2NO 2 - + 2H 2 O + 4H +, 2NO 2 + O 2 → 2NO 3 -), denitrification (facultative bacteria such as It has various functions such as (decomposing and removing nitric acid and nitrite), crushing, degeneration, and adsorption.
By nitrification dependent on aerobic microorganisms, ammonia nitrogen (NH 4 , NH 4 N) dissolved in the target water is converted to nitrogen gas (N 2 ) during the nitrification process and removed from the water, making it possible to reduce the chlorine injection rate. Become.
If necessary, denitrification that depends on facultative anaerobic microorganisms is also possible.
The electrolyzer may be selectively equipped with a submerged non-diaphragm type electrolyzer or a diaphragm type electrolyzer, and oxygen gas is generated from the anode and hydrogen gas is generated from the cathode in the passing water.
That is, the electrolytic device can instantly supply the required amount of oxygen gas and hydrogen gas to the target water in the required amount by electrolysis using the target water there as a raw material.
The electrolytic part is multi-stage dispersed and can be freely attached and detached to form an anaerobic environment and an aerobic environment in the area. This is different from the conventional so-called electrolytic levitation method for the purpose of solid-liquid separation, decolorization, oxidation, deodorization, etc., and the electrolytic device of the present invention is a means for providing an anaerobic and aerobic environment.

再び図3に戻って説明する。
すなわち生物ろ過処理工程Gのろ過池の次に物理的精密ろ過処理工程Hの精密ろ過池(前記ろ過池と区別するために「精密ろ過池」と称する)が設けられる。
物理的精密ろ過処理工程Hの入り口の電解装置(8)の機能とは、物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させる機能である。
図3に示す様に物理的精密ろ過処理工程Hの物理的精密ろ過装置(10)はセラミック製、焼結パーライト(黒曜石、真珠岩等由来)製、アルミナ製等の1〜2ミクロン(μm)の微細多孔のろ過板を有する。
該ろ過板はろ過面積を確保するために縦型波板、平板、円筒等が用いられ、単層または多層でもよい。
物理的精密ろ過処理工程Gに流入する水は既に浄化された浄水であるから目詰まりを強いる高水圧ろ過でなく水の水頭を用いる常圧ろ過が望ましい。
但し生物ろ過処理工程Gと同様に物理的精密ろ過処理工程Hの物理的精密ろ過装置(10)においても自動洗浄にするべきである。
また常時電解生成の有効塩素の作用による滅菌乃至除菌及び物理的洗浄は、自動化に貢献し効率的である。
This will be described by returning to FIG.
That is, next to the filtration pond in the biofiltration treatment step G, a precision filtration pond in the physical microfiltration treatment step H (referred to as a "microfiltration pond" to distinguish it from the filtration pond) is provided.
The function of the electrolyzer (8) at the entrance of the physical microfiltration process H is a function of generating chlorine for disinfection purposes at the entrance of the physical microfiltration process H.
As shown in FIG. 3, the physical precision filtration device (10) in the physical precision filtration process H is made of ceramic, sintered pearlite (derived from black stone, pearlite, etc.), alumina, etc., 1 to 2 microns (μm). It has a finely porous filter plate.
As the filtration plate, a vertical corrugated plate, a flat plate, a cylinder or the like is used to secure a filtration area, and may be a single layer or a multilayer.
Since the water flowing into the physical microfiltration treatment step G is already purified water, it is desirable to use atmospheric filtration using the water head instead of high water pressure filtration that causes clogging.
However, as in the biofiltration process G, the physical microfiltration device (10) in the physical microfiltration process H should also be automatically cleaned.
In addition, sterilization or sterilization and physical cleaning by the action of effective chlorine generated by electrolysis at all times contributes to automation and is efficient.

すなわち消毒目的の塩素についてこの電解装置(8)で発生させた塩素を用いるのであり、物理的精密ろ過処理工程Hの入り口において、消毒目的の塩素を発生させるものであった。
すなわち物理的精密ろ過処理工程Hの入り口において、流入する水は常時滅菌される。
この塩素の作用は物理的精密ろ過装置(10)の孔閉塞を防止し、ろ過継続時間を長くするだけでなく、該装置を経由した水に0.1mg/l乃至0.5mg/l程度等の残留塩素濃度(水道水として給水栓水で不足しない有効塩素を付与可能とするための残留塩素濃度)を与えることになる。
従来の緩速の「生物処理による浄化法(浄水処理法)」は大気と水面の接触のみで酸素を取り込んでいたが、電解装置は酸素を生成するから水面の面積を広くする必要がなくなり浄化設備の敷地を大幅に削減可能になる。
本考案の浄水処理の用途エリアとしては自由水面、タンク、管路等を選択可能であり、エリアの下層部を無酸素ゾーンにして嫌気性微生物による脱窒を可能にすることもできる。対象水の溶存酸素濃度、pH等は濃度計で検出して数値を自動制御してもよく、さらには流入時の生物学的酸素要求量の値でフィードフォワード制御等も可能である。
That is, the chlorine generated by the electrolyzer (8) is used for the chlorine for disinfection purposes, and the chlorine for disinfection purposes is generated at the entrance of the physical microfiltration treatment step H.
That is, at the entrance of the physical microfiltration process H, the inflowing water is always sterilized.
The action of chlorine not only prevents pore clogging of the physical precision filtration device (10) and prolongs the filtration duration, but also makes the water passing through the device about 0.1 mg / l to 0.5 mg / l, etc. Residual chlorine concentration (residual chlorine concentration to enable the addition of effective chlorine that is not insufficient in tap water as tap water) will be given.
The conventional slow-speed "purification method by biological treatment (water purification method)" takes in oxygen only by contact between the atmosphere and the water surface, but since the electrolyzer generates oxygen, it is not necessary to increase the area of the water surface and purify. The site of the equipment can be significantly reduced.
The free water surface, tank, pipeline, etc. can be selected as the application area for the water purification treatment of the present invention, and the lower part of the area can be set as an oxygen-free zone to enable denitrification by anaerobic microorganisms. The dissolved oxygen concentration, pH, etc. of the target water may be detected by a densitometer and the numerical values may be automatically controlled, and further, feedforward control or the like may be possible based on the value of the biological oxygen demand at the time of inflow.

次に図4乃至図6について説明する。
すなわち図3は本考案の浄水処理装置のろ過運転時の概念図であったが、図4は本考案の浄水処理装置の洗浄運転時の概念図である。
すなわち生物ろ過処理工程Gのろ過池と物理的精密ろ過処理工程Hの精密ろ過池のいずれも洗浄のために底部の弁が開けられて洗浄した水が下方に流れる様になっている。
図5は本考案の浄水処理装置の表面洗浄運転時の概念図であり、生物ろ過処理工程Gのろ過池と物理的精密ろ過処理工程Hの精密ろ過池の両者に設けられた噴水ノズル(12)から水が噴出し、その噴出水は縦型枠組構造体(3)と物理的精密ろ過装置(10)の表面に向けられてそれらの表面を洗浄する。
図6は本考案の浄水処理装置の逆流洗浄運転時の概念図であり、生物ろ過処理工程Gのろ過池の縦型枠組構造体(3)と物理的精密ろ過処理工程Hの精密ろ過池の物理的精密ろ過装置(10)の両者について、水が逆方向に流されて、それらが洗浄されるのである。
本考案の浄水処理装置に関連する考案、本考案とは独立した関連考案、をいくつか次に説明する。
まず第1の関連考案は「LED照明付き電解装置」という考案である。
この考案は微生物育成を促進するために、LED照明を電解装置に内蔵し太陽光が不足の場合に該LED光を点灯させるものである。
ここで電解装置が作動すれば必ず点灯する「LED照明」と、電解装置とは独立してLED光を点灯させる「LED照明」という2種の方式がある。
従来浄水処理装置に使用する酸素生成機能を有する電解装置として「LED照明付き電解装置」なるものは全く存在しなかった。
次に第2の関連考案は過剰プランクトン、バクテリア残渣等は電解装置で酸素を発生させる等の運転時に例えば酸素が浮上する際に、過剰プランクトン、バクテリア残渣等が酸素と一緒に上昇する(傾向がある)ことになる。
従って電解装置の酸素発生等の運転により過剰プランクトン、バクテリア残渣等がろ過池の水面に集まることになる。
従って電解装置の酸素発生等の運転時には、ろ過池(精密ろ過池があればそれも)を常時オーバーフロー状態にすれば、過剰プランクトン、バクテリア残渣等が排出されて、それらによる「ろ過設備」のろ過抵抗の増加を防止しその洗浄周期を長くすることができる。すなわち第2の関連考案は『電解装置の酸素発生等の運転時にろ過池を常時オーバーフロー状態にする』という考案である。
これによって過剰プランクトン、バクテリア残渣等による「ろ過設備」のろ過抵抗の増加を防止し、その洗浄周期を長くすることができる。
またオーバーフローさせる場合は、そのフロー水の99.9%は原水に戻すためそのフロー水は調整槽に入れて、そこで過剰プランクトン、バクテリア残渣等を沈殿除去した後に、その上澄水を原水に戻せばよい。
Next, FIGS. 4 to 6 will be described.
That is, FIG. 3 is a conceptual diagram of the water purification apparatus of the present invention during the filtration operation, while FIG. 4 is a conceptual diagram of the water purification apparatus of the present invention during the cleaning operation.
That is, in both the filtration pond of the biological filtration treatment step G and the precision filtration pond of the physical microfiltration treatment step H, the valve at the bottom is opened for cleaning so that the washed water flows downward.
FIG. 5 is a conceptual diagram of the water purification apparatus of the present invention during the surface cleaning operation, and is a fountain nozzle (12) provided in both the filtration pond in the biological filtration treatment step G and the precision filtration pond in the physical microfiltration treatment step H. ), Which is directed toward the surfaces of the vertical framework structure (3) and the physical microfiltration device (10) to clean their surfaces.
FIG. 6 is a conceptual diagram of the water purification apparatus of the present invention during the backflow cleaning operation of the vertical frame structure (3) of the filtration pond in the biofiltration treatment step G and the precision filtration pond in the physical microfiltration treatment step H. For both physical microfiltration devices (10), water is flowed in opposite directions to wash them.
The following describes some devices related to the water purification apparatus of the present invention and related devices independent of the present invention.
First, the first related device is a device called "electrolyzer with LED lighting".
In this invention, in order to promote the growth of microorganisms, LED lighting is built in an electrolytic device to turn on the LED light when sunlight is insufficient.
Here, there are two types of methods, "LED lighting" that lights up whenever the electrolytic device operates, and "LED lighting" that lights the LED light independently of the electrolytic device.
Conventionally, there has been no "LED-lit electrolyzer" as an electrolyzer having an oxygen generating function used in a water purification device.
Next, the second related device is that excess plankton, bacterial residue, etc. rise together with oxygen during operation such as generating oxygen in an electrolytic device, for example, when oxygen floats. There is).
Therefore, excess plankton, bacterial residue, etc. will collect on the water surface of the filtration pond due to the operation of oxygen evolution of the electrolyzer.
Therefore, if the filtration pond (if there is a microfiltration pond, if any) is constantly overflowed during operation such as oxygen evolution of the electrolyzer, excess plankton, bacterial residue, etc. will be discharged, and filtration of the "filtration equipment" by them The increase in resistance can be prevented and the cleaning cycle can be lengthened. That is, the second related device is a device that "the filtration pond is always in an overflow state during operation such as oxygen evolution of the electrolytic device".
This makes it possible to prevent an increase in the filtration resistance of the "filtration equipment" due to excess plankton, bacterial residues, etc., and to prolong the cleaning cycle.
In the case of overflow, 99.9% of the flow water is returned to the raw water, so the flow water is placed in a conditioning tank, where excess plankton, bacterial residues, etc. are precipitated and removed, and then the supernatant water is returned to the raw water. Good.

本考案の浄水処理装置は、「生物処理による浄化法(浄水処理法)」の原理を用いながらも省スペース化を実現することができることから、浄水処理装置の産業分野において有用であり、産業上の利用可能性が大きい。 Since the water purification device of the present invention can realize space saving while using the principle of "purification method by biological treatment (water purification method)", it is useful in the industrial field of the water purification device and is industrially effective. Is highly available.

1 浄水工程
2 浄水処理装置
3 縦型枠組構造体
4 容器状構造体
5 担体
6 電解装置
7 接続路
8 電解装置
10 物理的精密ろ過装置
11 孔
12 噴射ノズル
90 前段工程
1 Water purification process 2 Water purification device 3 Vertical frame structure 4 Container-like structure 5 Carrier 6 Electrolyzer 7 Connection path 8 Electrolyzer 10 Physical precision filtration device 11 holes 12 Injection nozzle 90 Pre-stage process

本考案の第1の目的は「Jシンプソンの緩速ろ過法」または「生物処理による浄化法(浄水処理法)」の原理を用いながらも省スペースにすることであり、本考案の第2の目的は生物膜の管理の省力化であり、本考案の第3の目的はろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し浄水処理の安全性を確実にさせる、以上の3つを目的とする。
以上の3つの目的について以下分説する:
本考案の第1の目的は、上記の従来の急速ろ過法の問題点を解決すべく、「生物処理による浄化法(浄水処理法)」の原理を用い、それを構造的に改良して「生物処理による浄化法(浄水処理法)」のさらなる実用化を図るものである。
すなわちその改良点とは、従来の「生物処理による浄化法(浄水処理法)」においては「ろ過水量」が水平な砂層の平面積(表面負荷率)を基準としているが、その砂層を水平でなく「縦配置」にすることにより省スペースにすることが可能になるのであるが、この「縦配置」は生物膜を構成する好気性微生物への酸素の供給という点から従来は困難とされていたのを、本考案は簡単な電気分解装置(電解装置)を付加することにより解決したのである。
すなわち従来は大気と接する「ろ過池」の水面積から微生物に必要な酸素を大気中から取り込んでいるので、「縦配置」にすれば水面積が縮小され、当然のことながら酸素が不足になる。
その解決方法として本考案では、請求項3乃至5の考案に限定されるが、電気分解装置(電解装置)を付加することにしたのである。
次に本考案の第2の目的は、「生物処理による浄化法(浄水処理法)」における重要な問題であった生物膜の維持管理を省力化及び効率化することにある。
この第2の目的達成のために、まず「生物膜」の構造乃至構成を改良した、その詳細は後述する。
次に省力化及び効率化のために、請求項1乃至3の考案に限定されるが、それらの「電解装置」を酸素供給だけでなく塩素供給も可能にし、そしてそれら選択切り替え可能にし、生物膜の維持管理の省力化及び効率化のための主要な役割を「電解装置」に持たせたのである。
さらに省力化及び効率化のために、具体的構成の詳細は後述するが、「生物膜」の構成(該「生物膜」を複数の構成とし、そのひとつ)として「流動する浮遊担体」なるものを用いて、それが流動することによる物理的作用を生物膜の維持管理の省力化及び効率化に用いたのである。
The first object of the present invention is to save space while using the principle of "J Simpson's slow sand filtration method" or "purification method by biological treatment (water purification method)", and the second purpose of the present invention is to save space. The purpose is to save labor in the management of biological membranes, and the third purpose of the present invention is to add a microporous physical microfiltration treatment step as the next step of the filtration pond to ensure the safety of water purification treatment. The purpose is three.
The above three purposes are explained below:
The first object of the present invention is to use the principle of "purification method by biological treatment (water purification method)" and structurally improve it in order to solve the above-mentioned problems of the conventional rapid filtration method. This is to further put into practical use the "purification method by biological treatment (water purification method)".
That is, the improvement point is that in the conventional "purification method by biological treatment (water purification method)", the "filtered water amount" is based on the horizontal area (surface load factor) of the horizontal sand layer, but the sand layer is horizontal. It is possible to save space by using "vertical arrangement" instead, but this "vertical arrangement" has been considered difficult in the past in terms of supplying oxygen to the aerobic microorganisms that make up the biofilm. However, the present invention was solved by adding a simple electrolyzer (electrolyzer).
In other words, conventionally, oxygen required for microorganisms is taken in from the atmosphere from the water area of the "filtration pond" that is in contact with the atmosphere, so if it is "vertically arranged", the water area will be reduced and, of course, oxygen will be insufficient. ..
As a solution to this problem, the present invention is limited to the inventions of claims 3 to 5 , but an electrolyzer (electrolyzer) is added.
Next, the second object of the present invention is to save labor and improve the efficiency of maintenance of biofilm, which has been an important problem in the "purification method by biological treatment (water purification method)".
In order to achieve this second purpose, the structure or composition of the "biofilm" was first improved, the details of which will be described later.
Next, for labor saving and efficiency improvement, although limited to the inventions of claims 1 to 3, those "electrolyzers" can supply not only oxygen but also chlorine, and can switch between them, and biofilms. The "electrolyzer" was given the main role of labor saving and efficiency improvement of the maintenance of the film.
Further, in order to save labor and improve efficiency, the details of the specific configuration will be described later, but the configuration of the "biofilm" (the "biofilm" has a plurality of configurations and one of them) is a "flowing floating carrier". Was used to save labor and improve efficiency in the maintenance of biofilms by using the physical action of the flow of the biofilm.

以下各々について説明する。
まず「生物膜(生物ろ過膜)」であるが、これは以下の2つの構成からなり:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された砂等の多様なろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重の多孔質体等の生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の2つで構成される。
前記第2の担体については、その浮遊状態の制御により、前記第1の生物ろ過膜の状態を最適化するために用いることが可能になる。
次に、請求項3乃至5の考案に限定されるが、その「電解装置」について説明すれば、その設置位置は大きく分類して2つの設置位置があり、
まず第1の設置位置は、ろ過池において縦型枠組構造体の間(ある間隔で設置される場合はそれらのゾーンの間)の水中に、該水中の上下方向は任意(例えば底部、中部等)に選択可能に設置される。
次に第2の設置位置は、生物膜によるろ過工程の後であり、かつ次の工程である精密ろ過工程の入り口において、消毒目的の塩素を発生させるために、ここにも電解装置が設置される。
従って、まずろ過池の電解装置について説明し、その後に精密ろ過工程の入り口の電解装置について説明する。
すなわち、ろ過池の電解装置の第1の機能としては、これで生成される酸素ガスを水中に生成溶存させることで微生物の硝化、脱窒、食物連鎖の活性化を図る。
Each will be described below.
The first is "biofilm (biofiltration membrane)", which consists of the following two configurations:
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various filter media layers such as sand stored in the structure (because it is a container). Biofilm composed of microorganisms The second is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place such as a porous body having a specific gravity similar to that of water, and is abundant in the water of a filtration pond. It is composed of the above two that exist in a fluid state.
By controlling the floating state of the second carrier, it becomes possible to use it for optimizing the state of the first biofiltration membrane.
Next, although limited to the inventions of claims 3 to 5 , if the "electrolyzer" is described, the installation positions are roughly classified into two installation positions.
First, the first installation position is in the water between the vertical frame structures (between those zones when installed at a certain interval) in the filtration pond, and the vertical direction of the water is arbitrary (for example, bottom, middle, etc.). ) Can be selected.
Next, the second installation position is after the biofilm filtration process, and at the entrance of the microfiltration process, which is the next process, an electrolytic device is also installed here in order to generate chlorine for disinfection purposes. To.
Therefore, the electrolyzer of the filtration pond will be described first, and then the electrolyzer at the entrance of the microfiltration step will be described.
That is, the first function of the electrolytic device of the filtration pond is to nitrify, denitrify, and activate the food chain of microorganisms by generating and dissolving the oxygen gas generated by the electrolytic device in water.

本考案は以上の目的達成のために:
請求項1として、濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池の水中に、容器状に構成される複数の縦型枠組構造体を備えると共に、前記縦型枠組構造体は、縦型枠組構造体の外面に微生物が生息して構成される生物膜と、縦型枠組構造体内(容器になっているから容器内)に収納された多様な単層または複数層設けられたろ材層に微生物が生息して構成される生物膜とを有し、前記縦型枠組構造体の外面に有する生物膜と、前記縦型枠組構造体内に有する生物膜とに前記処理水または前記濁質濃度が10mg/l以下の原水を接触させる、以上の浄水処理装置を提案するものである。
請求項2として、請求項1の特徴に加えて、ろ過池の水中における複数の縦型枠組構造体の相互の間に、水と同程度の比重であって、濁度を低くする処理をされた処理水中または濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される担体を多数流動状態で存在させて備えると共に、前記担体は、生物居所となる担体に微生物が生息して構成される生物膜を有し、前記生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させる、以上の浄水処理装置を提案するものである。
請求項3として、請求項1又は2の特徴に加えて、ろ過池の水中に、前記水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を備える、以上の浄水処理装置を提案するものである。
請求項4として、請求項2又は3の特徴に加えて、縦側枠組構造体に有する生物膜と、担体に有する生物膜とに接触した濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水が流入して接触する位置に、微細多孔のろ過板を有する物理的精密ろ過装置を備える、以上の浄水処理装置を提案するものである。
請求項5として、請求項2又は3の特徴に加えて、縦側枠組構造体に有する生物膜と、担体に有する生物膜とに接触した濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水が流入して接触する位置で、且つ前記処理水または前記原水が物理的精密ろ過装置と接触するよりも前の位置に、消毒目的の塩素を発生させる電解装置を設ける、以上の浄水処理装置を提案するものである。
The present invention aims to achieve the above objectives:
According to claim 1, it is a water purification device that purifies treated water that has been treated to reduce turbidity or raw water having a turbidity concentration of 10 mg / l or less, and is configured in a container shape in the water of a filtration pond. The vertical frame structure is provided with a plurality of vertical frame structures, and the vertical frame structure includes a biological membrane composed of microorganisms inhabiting the outer surface of the vertical frame structure and a vertical frame structure (as a container). It has a biological film formed by inhabiting microorganisms in various single-layer or multiple-layered filter medium layers stored in the container), and has a biological film on the outer surface of the vertical frame structure. The present invention proposes the above water purification apparatus in which the treated water or the raw water having a turbidity concentration of 10 mg / l or less is brought into contact with the biological film contained in the vertical framework structure .
As a second aspect, in addition to the feature of the first aspect, a treatment is performed between a plurality of vertical framework structures in the water of the filtration pond to reduce the turbidity with a specific gravity similar to that of water. A large number of carriers formed of porous bodies that can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less are present in a fluid state, and the carriers are carriers that serve as biological residences. It is proposed the above water purification apparatus which has a biological membrane composed of microorganisms inhabiting the water, and brings the treated water or raw water having a turbidity concentration of 10 mg / l or less into contact with the biological membrane .
As a third aspect, in addition to the features of the first or second aspect, the above water purification apparatus provided with an electrolyzer (electrolyzer) in the water of the filtration pond so that the vertical direction of the water can be arbitrarily selected. It is a suggestion.
As a fourth aspect, in addition to the features of the second or third aspect, the treated water or turbidity which has been treated to reduce the turbidity in contact with the biological membrane of the vertical framework structure and the biological membrane of the carrier. The above-mentioned water purification apparatus is proposed, which is provided with a physical microfiltration apparatus having a microporous filtration plate at a position where raw water having a concentration of 10 mg / l or less flows in and comes into contact with the raw water.
As a fifth aspect, in addition to the features of the second or third aspect, the treated water or turbidity which has been treated to reduce the turbidity in contact with the biological membrane of the vertical framework structure and the biological membrane of the carrier. An electrolytic device that generates chlorine for disinfection purposes is installed at a position where raw water having a concentration of 10 mg / l or less flows in and contacts, and at a position before the treated water or the raw water comes into contact with a physical microfiltration device. It proposes the above water purification equipment to be provided.

本考案の第1の目的は「Jシンプソンの緩速ろ過法」または「生物処理による浄化法(浄水処理法)」の原理を用いながらも省スペースにすることであり、本考案の第2の目的は生物膜の管理の省力化であり、本考案の第3の目的はろ過池の次の工程として微細多孔の物理的精密ろ過処理工程を付加し浄水処理の安全性を確実にさせる、以上の3つを目的とする。
以上の3つの目的について以下分説する:
本考案の第1の目的は、上記の従来の急速ろ過法の問題点を解決すべく、「生物処理による浄化法(浄水処理法)」の原理を用い、それを構造的に改良して「生物処理による浄化法(浄水処理法)」のさらなる実用化を図るものである。
すなわちその改良点とは、従来の「生物処理による浄化法(浄水処理法)」においては「ろ過水量」が水平な砂層の平面積(表面負荷率)を基準としているが、その砂層を水平でなく「縦配置」にすることにより省スペースにすることが可能になるのであるが、この「縦配置」は生物膜を構成する好気性微生物への酸素の供給という点から従来は困難とされていたのを、本考案は簡単な電気分解装置(電解装置)を付加することにより解決したのである。
すなわち従来は大気と接する「ろ過池」の水面積から微生物に必要な酸素を大気中から取り込んでいるので、「縦配置」にすれば水面積が縮小され、当然のことながら酸素が不足になる。
その解決方法として本考案では、請求項3乃至5の考案に限定されるが、電気分解装置(電解装置)を付加することにしたのである。
次に本考案の第2の目的は、「生物処理による浄化法(浄水処理法)」における重要な問題であった生物膜の維持管理を省力化及び効率化することにある。
この第2の目的達成のために、まず「生物膜」の構造乃至構成を改良した、その詳細は後述する。
次に省力化及び効率化のために、請求項1乃至3の考案に限定されるが、それらの「電解装置」を酸素供給だけでなく塩素供給も可能にし、そしてそれら選択切り替え可能にし、生物膜の維持管理の省力化及び効率化のための主要な役割を「電解装置」に持たせたのである。
さらに省力化及び効率化のために、具体的構成の詳細は後述するが、「生物膜」の構成(該「生物膜」を複数の構成とし、そのひとつ)として「流動する浮遊担体」なるものを用いて、それが流動することによる物理的作用を生物膜の維持管理の省力化及び効率化に用いたのである。
The first object of the present invention is to save space while using the principle of "J Simpson's slow sand filtration method" or "purification method by biological treatment (water purification method)", and the second purpose of the present invention is to save space. The purpose is to save labor in the management of biological membranes, and the third purpose of the present invention is to add a microporous physical microfiltration treatment step as the next step of the filtration pond to ensure the safety of water purification treatment. The purpose is three.
The above three purposes are explained below:
The first object of the present invention is to use the principle of "purification method by biological treatment (water purification method)" and structurally improve it in order to solve the above-mentioned problems of the conventional rapid filtration method. This is to further put into practical use the "purification method by biological treatment (water purification method)".
That is, the improvement point is that in the conventional "purification method by biological treatment (water purification method)", the "filtered water amount" is based on the horizontal area (surface load factor) of the horizontal sand layer, but the sand layer is horizontal. It is possible to save space by using "vertical arrangement" instead, but this "vertical arrangement" has been considered difficult in the past in terms of supplying oxygen to the aerobic microorganisms that make up the biofilm. However, the present invention was solved by adding a simple electrolyzer (electrolyzer).
In other words, conventionally, oxygen required for microorganisms is taken in from the atmosphere from the water area of the "filtration pond" that is in contact with the atmosphere, so if it is "vertically arranged", the water area will be reduced and, of course, oxygen will be insufficient. ..
As a solution to this problem, the present invention is limited to the inventions of claims 3 to 5 , but an electrolyzer (electrolyzer) is added.
Next, the second object of the present invention is to save labor and improve the efficiency of maintenance of biofilm, which has been an important problem in the "purification method by biological treatment (water purification method)".
In order to achieve this second purpose, the structure or composition of the "biofilm" was first improved, the details of which will be described later.
Next, for labor saving and efficiency improvement, although limited to the inventions of claims 1 to 3, those "electrolyzers" can supply not only oxygen but also chlorine, and can switch between them, and biofilms. The "electrolyzer" was given the main role of labor saving and efficiency improvement of the maintenance of the film.
Further, in order to save labor and improve efficiency, the details of the specific configuration will be described later, but the configuration of the "biofilm" (the "biofilm" has a plurality of configurations and one of them) is a "flowing floating carrier". Was used to save labor and improve efficiency in the maintenance of biofilms by using the physical action of the flow of the biofilm.

以下各々について説明する。
まず「生物膜(生物ろ過膜)」であるが、これは以下の2つの構成からなり:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された砂等の多様なろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重の多孔質体等の生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の2つで構成される。
前記第2の担体については、その浮遊状態の制御により、前記第1の生物ろ過膜の状態を最適化するために用いることが可能になる。
次に、請求項3乃至5の考案に限定されるが、その「電解装置」について説明すれば、その設置位置は大きく分類して2つの設置位置があり、
まず第1の設置位置は、ろ過池において縦型枠組構造体の間(ある間隔で設置される場合はそれらのゾーンの間)の水中に、該水中の上下方向は任意(例えば底部、中部等)に選択可能に設置される。
次に第2の設置位置は、生物膜によるろ過工程の後であり、かつ次の工程である精密ろ過工程の入り口において、消毒目的の塩素を発生させるために、ここにも電解装置が設置される。
従って、まずろ過池の電解装置について説明し、その後に精密ろ過工程の入り口の電解装置について説明する。
すなわち、ろ過池の電解装置の第1の機能としては、これで生成される酸素ガスを水中に生成溶存させることで微生物の硝化、脱窒、食物連鎖の活性化を図る。
Each will be described below.
The first is "biofilm (biofiltration membrane)", which consists of the following two configurations:
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various filter media layers such as sand stored in the structure (because it is a container). Biofilm composed of microorganisms The second is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place such as a porous body having a specific gravity similar to that of water, and is abundant in the water of a filtration pond. It is composed of the above two that exist in a fluid state.
By controlling the floating state of the second carrier, it becomes possible to use it for optimizing the state of the first biofiltration membrane.
Next, although limited to the inventions of claims 3 to 5 , if the "electrolyzer" is described, the installation positions are roughly classified into two installation positions.
First, the first installation position is in the water between the vertical frame structures (between those zones when installed at a certain interval) in the filtration pond, and the vertical direction of the water is arbitrary (for example, bottom, middle, etc.). ) Can be selected.
Next, the second installation position is after the biofilm filtration process, and at the entrance of the microfiltration process, which is the next process, an electrolytic device is also installed here in order to generate chlorine for disinfection purposes. To.
Therefore, the electrolyzer of the filtration pond will be described first, and then the electrolyzer at the entrance of the microfiltration step will be described.
That is, the first function of the electrolytic device of the filtration pond is to nitrify, denitrify, and activate the food chain of microorganisms by generating and dissolving the oxygen gas generated by the electrolytic device in water.

本考案は以上の目的達成のために:
請求項1として、濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池の水中に、容器状に構成される複数の縦型枠組構造体を備えると共に、前記縦型枠組構造体は、縦型枠組構造体の外面に微生物が生息して構成される生物膜と、縦型枠組構造体内に収納された単層または複数層設けられたろ材層に微生物が生息して構成される生物膜とを有し、前記縦型枠組構造体の外面に有する生物膜と、前記縦型枠組構造体内に有する生物膜とに前記処理水または前記濁質濃度が10mg/l以下の原水を接触させる、以上の浄水処理装置を提案するものである。
請求項2として、請求項1の特徴に加えて、ろ過池の水中における複数の縦型枠組構造体の相互の間に、水と同程度の比重であって、濁度を低くする処理をされた処理水中または濁質濃度が10mg/l以下の原水中に多孔質体で形成される担体を多数備えると共に、前記担体は、生物居所となる担体に微生物が生息して構成される生物膜を有し、前記生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させる、以上の浄水処理装置を提案するものである。
請求項3として、請求項1又は2の特徴に加えて、ろ過池の水中に、前記水中の上下方向は任意に選択可能に、電気分解装置を備える、以上の浄水処理装置を提案するものである。
請求項4として、請求項2又は3の特徴に加えて、縦側枠組構造体に有する生物膜と、担体に有する生物膜とに接触した濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水が流入して接触する位置に、微細多孔のろ過板を有する物理的精密ろ過装置を備える、以上の浄水処理装置を提案するものである。
請求項5として、請求項2又は3の特徴に加えて、縦側枠組構造体に有する生物膜と、担体に有する生物膜とに接触した濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水が流入して接触する位置で、且つ前記処理水または前記原水が物理的精密ろ過装置と接触するよりも前の位置に、消毒目的の塩素を発生させる電解装置を設ける、以上の浄水処理装置を提案するものである。
The present invention aims to achieve the above objectives:
According to claim 1, it is a water purification device that purifies treated water that has been treated to reduce turbidity or raw water having a turbidity concentration of 10 mg / l or less, and is configured in a container shape in the water of a filtration pond. The vertical frame structure is provided with a plurality of vertical frame structures, and the vertical frame structure includes a biological membrane composed of microorganisms inhabiting the outer surface of the vertical frame structure and a single body housed in the vertical frame structure. A biological membrane composed of microorganisms inhabiting a layer or a filter medium layer provided in a plurality of layers, a biological membrane having an outer surface of the vertical framework structure, and a biological membrane having a biological membrane inside the vertical framework structure. The above-mentioned water purification apparatus is proposed in which the treated water or the raw water having a turbidity concentration of 10 mg / l or less is brought into contact with the water.
As a second aspect, in addition to the feature of the first aspect, a treatment is performed between a plurality of vertical framework structures in the water of the filtration pond to reduce the turbidity with a specific gravity similar to that of water. It is provided with a large number of carriers formed of a porous body in the treated water or raw water having a turbidity concentration of 10 mg / l or less, and the carrier is a biological membrane composed of microorganisms inhabiting the carrier that serves as a biological residence. The present invention proposes the above-mentioned water purification apparatus, which has the treated water or the raw water having a turbidity concentration of 10 mg / l or less in contact with the biological membrane .
As a third aspect, in addition to the features of the first or second aspect, the above water purification apparatus is provided with an electrolyzer in the water of the filtration pond so that the vertical direction of the water can be arbitrarily selected. is there.
As a fourth aspect, in addition to the features of the second or third aspect, the treated water or turbidity which has been treated to reduce the turbidity in contact with the biological membrane of the vertical framework structure and the biological membrane of the carrier. The above-mentioned water purification apparatus is proposed, which is provided with a physical microfiltration apparatus having a microporous filtration plate at a position where raw water having a concentration of 10 mg / l or less flows in and comes into contact with the raw water.
As a fifth aspect, in addition to the features of the second or third aspect, the treated water or turbidity which has been treated to reduce the turbidity in contact with the biological membrane of the vertical framework structure and the biological membrane of the carrier. An electrolytic device that generates chlorine for disinfection purposes is installed at a position where raw water having a concentration of 10 mg / l or less flows in and contacts, and at a position before the treated water or the raw water comes into contact with a physical microfiltration device. It proposes the above water purification equipment to be provided.

Claims (8)

濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設けた、以上の浄水処理装置
A water purification device that purifies treated water that has been treated to reduce turbidity or raw water with a turbidity concentration of 10 mg / l or less, and is a biofilm provided in a filtration pond.
The first is a biofilm composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biofilm, which is composed of microorganisms inhabiting the filter medium layer, has a specific gravity similar to that of water and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biofilm composed of microorganisms inhabiting a carrier that serves as a living place formed of a porous body, and is used as a first and second biofilm that is present in a large number of fluid states in the water of a filtration pond. The treated water or raw water having a turbidity concentration of 10 mg / l or less was brought into contact with the water, and then an electrolysis device (electrolytic device) was provided in the water of the filtration pond so that the vertical direction of the water could be arbitrarily selected. , Above water purification equipment
濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設け、前記ろ過池の次の工程として微細多孔の物理的精密ろ過工程を付加した、以上の浄水処理装置
A water purification device that purifies treated water that has been treated to reduce turbidity or raw water with a turbidity concentration of 10 mg / l or less, and is a biofilm provided in a filtration pond.
The first is a biological membrane composed of microorganisms inhabiting the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biological membrane composed of microorganisms inhabiting the filter medium layer has a specific gravity similar to that of water, and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biological membrane composed of microorganisms inhabiting a carrier that serves as a living place formed of a porous body, and is a first and second biological membrane that is present in a large number of fluid states in the water of a filtration pond. The treated water or the raw water having a turbidity concentration of 10 mg / l or less is brought into contact with the water, and then an electrolysis device (electrolytic device) is provided in the water of the filtration pond so that the vertical direction of the water can be arbitrarily selected. The above water purification device to which a microporous physical microfiltration step is added as the next step of the filtration pond.
濁度を低くする処理をされた処理水または濁質濃度が10mg/l以下の原水の浄水処理を行う浄水処理装置であって、ろ過池に設けられた生物膜、該生物膜とは:
第1は容器状の縦型枠組構造体の外面に微生物が生息して構成される生物膜と該構造体内(容器になっているから容器内)に収納された多様な単層または複層設けられたろ材層に微生物が生息して構成される生物膜
第2は水と同程度の比重であって、前記処理水中または前記濁質濃度が10mg/l以下の原水中に浮遊状態で存在可能な多孔質体で形成される生物居所となる担体に微生物が生息して構成される生物膜であり、ろ過池の水中に多数流動状態で存在させるもの
以上の第1と第2の生物膜に前記処理水または前記濁質濃度が10mg/l以下の原水を接触させ、次に前記ろ過池の水中に、該水中の上下方向は任意に選択可能に、電気分解装置(電解装置)を設け、前記ろ過池の次の工程として微細多孔の物理的精密ろ過工程を付加し、次に前記生物膜によるろ過工程の後であり、かつ前記微細多孔の物理的精密ろ過工程の入り口において、消毒目的の塩素を発生させる電解装置を設けた、以上の浄水処理装置
A water purification device that purifies treated water that has been treated to reduce turbidity or raw water with a turbidity concentration of 10 mg / l or less, and is a biofilm provided in a filtration pond.
The first is a biological membrane formed by inhabiting microorganisms on the outer surface of a container-shaped vertical frame structure and various single-layer or multi-layers housed in the structure (because it is a container). The second biological membrane composed of microorganisms inhabiting the filter medium layer has a specific gravity similar to that of water, and can exist in a suspended state in the treated water or raw water having a turbidity concentration of 10 mg / l or less. It is a biological membrane composed of microorganisms inhabiting a carrier that serves as a biological residence formed of a porous body, and is a first and second biological membrane that is present in a large number of fluid states in the water of a filtration pond. The treated water or the raw water having a turbidity concentration of 10 mg / l or less is brought into contact with the water, and then an electrolysis device (electrolytic device) is provided in the water of the filtration pond so that the vertical direction of the water can be arbitrarily selected. A microporous physical precision filtration step is added as the next step of the filtration pond, and then after the microporous physical precision filtration step and at the entrance of the microporous physical precision filtration step, for disinfection purposes. The above water purification device equipped with an electrolytic device that generates chlorine
請求項2について微細多孔の物理的精密ろ過工程の入り口の電解装置に代えて、その酸素供給手段としての電解装置の機能の代用としてポンプによる散水、水中キャビテーション、(空気の)マイクロバブリングで置換した浄水処理装置 Regarding claim 2, instead of the electrolyzer at the entrance of the microporous physical microfiltration process, the function of the electrolyzer as an oxygen supply means was replaced by watering by a pump, underwater cavitation, or micro bubbling (of air). Water purification equipment 請求項3について微細多孔の物理的精密ろ過工程の入り口の電解装置に代えて、その消毒手段としての電解装置の機能の代用として直接塩素注入で置換した浄水処理装置 Regarding claim 3, instead of the electrolyzer at the entrance of the microporous physical microfiltration process, the water purification device is directly replaced by chlorine injection as a substitute for the function of the electrolyzer as a disinfecting means. 請求項3について微細多孔の物理的精密ろ過工程の入り口の電解装置に代えて、その消毒手段としての電解装置の機能の代用として物理的精密ろ過装置について超音波洗浄で置換した浄水処理装置 Regarding claim 3, instead of the electrolyzer at the entrance of the microporous physical microfiltration process, the physical microfiltration device is replaced by ultrasonic cleaning as a substitute for the function of the electrolyzer as a disinfecting means. LED照明付きにした電解装置を用いた請求項1、2、3、4、5、6の浄水処理装置 The water purification apparatus according to claim 1, 2, 3, 4, 5, 6 using an electrolyzer equipped with LED lighting. 電解装置の酸素発生等の運転時にろ過池を常時オーバーフロー状態にする請求項1、2、3、4、5、6の浄水処理装置 The water purification apparatus according to claim 1, 2, 3, 4, 5, 6 that constantly overflows the filtration pond during operation such as oxygen evolution of the electrolytic apparatus.
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JP7422304B1 (en) 2022-10-14 2024-01-26 好包 生武 Three-dimensional slow filtration

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7422304B1 (en) 2022-10-14 2024-01-26 好包 生武 Three-dimensional slow filtration

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