JP5286475B2 - High concentration wastewater treatment system - Google Patents

High concentration wastewater treatment system Download PDF

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JP5286475B2
JP5286475B2 JP2010138727A JP2010138727A JP5286475B2 JP 5286475 B2 JP5286475 B2 JP 5286475B2 JP 2010138727 A JP2010138727 A JP 2010138727A JP 2010138727 A JP2010138727 A JP 2010138727A JP 5286475 B2 JP5286475 B2 JP 5286475B2
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信夫 菊池
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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Description

本発明は、自然界微生物の相互作用を利用した高能力の生物処理を達成する高濃度排水処理システムに関する。The present invention relates to a high-concentration wastewater treatment system that achieves high-performance biological treatment utilizing the interaction of natural microorganisms.

従来から排水処理技術に用いられる生物学的処理方法は生物処理の中の活性汚泥法が多く、又実際に実施されている。Conventionally, biological treatment methods used in wastewater treatment technology are many activated sludge methods in biological treatment, and are actually implemented.

その活性汚泥法は主に好気性菌を使い溶存酸素を消費し、菌体培養を繰り返しながら有機物の低分子化をし、水と二酸化炭素と窒素とリン等に分解する。一方、嫌気性菌利用分野では溶存酸素が無くなると、硝酸イオンNO の酸素を利用する菌も活動して窒素ガスと酸素に分解する。又硫化水素HSの水素を還元剤として利用する微生物により無害化すると共に臭気を断ち更に汚泥減量化に効果を発揮する。よって好気性処理と嫌気性処理を併用する例も提案されている(特許文献1)。The activated sludge method mainly uses aerobic bacteria, consumes dissolved oxygen, reduces the molecular weight of organic matter while repeating cell culture, and decomposes it into water, carbon dioxide, nitrogen, phosphorus, and the like. On the other hand, in the anaerobic bacteria utilization field, when dissolved oxygen disappears, bacteria utilizing the oxygen of nitrate ion NO 3 also act and decompose into nitrogen gas and oxygen. In addition, it is detoxified by microorganisms using hydrogen sulfide H 2 S as a reducing agent, and is also effective in reducing sludge by cutting off odor. Therefore, an example in which aerobic treatment and anaerobic treatment are used in combination has also been proposed (Patent Document 1).

従来の生物処理での活性汚泥法では流入する有機物量に対応する微生物群の増殖が充分でないと希薄な生物槽となる。その場合槽内の低分子化が進まず原生動物も少なくなり、沈殿槽でのバルキング現象の原因となる。この為凝集剤添加によるフロック沈降を計っている。微生物の循環機能が働く場合は菌類により発せられた酵素が汚泥を集めフロック化できる。その活動を終止させ沈降させるのが後生動物であり、沈降速度は速くしかも高密度となる。微生物間の食物連鎖による循環は一番重要であり、その中の一部分が欠落すると、全体に悪影響を及ぼし対応する能力が弱く環境に順応できない。槽内の随所にpH調整の薬液が多く使用されている。本来順調に活動する微生物群の相互培養作用が確立している場合は、pHの少々の高低があっても微生物が自ら活動しやすいpH環境を造る能力があり、薬液は必要としない。In the activated sludge method in the conventional biological treatment, if the growth of the microorganism group corresponding to the amount of inflowing organic matter is not sufficient, it becomes a dilute biological tank. In that case, the molecular weight in the tank does not progress and the number of protozoa also decreases, causing a bulking phenomenon in the sedimentation tank. For this reason, floc sedimentation by adding a flocculant is measured. When the circulatory function of microorganisms works, enzymes emitted by fungi can collect sludge and flock it. It is metazoans that terminate and sink their activity, and the sedimentation rate is fast and dense. Circulation by the food chain between microorganisms is the most important, and if a part of it is missing, the whole will be adversely affected and the ability to respond is weak, making it impossible to adapt to the environment. Many chemicals for pH adjustment are used everywhere in the tank. In the case where the mutual culture action of microorganism groups that normally operate smoothly has been established, there is the ability to create a pH environment in which microorganisms can easily act even if the pH is slightly high and low, and no chemical solution is required.

又、好気性菌と嫌気性菌の併用活用を目的とした、天然鉱石濾材を散水濾床とする提案があり、生物処理に於いて微生物の相互作用を促す方法が記載されている(特許文献2)。In addition, there is a proposal to use a natural ore filter medium as a sprinkling filter for the purpose of combined use of aerobic bacteria and anaerobic bacteria, and a method for promoting the interaction of microorganisms in biological treatment is described (Patent Document) 2).

特許文献2は流入廃水の生物化学的酸素要求量BOD3,000ppmを下回る場合に於いて槽の上部を開放した形態で成立している。このシステムは開口部を閉鎖した場合は微生物の循環機能に大きな欠落が生じる。食物連鎖でのバランスが崩れると生物処理全体に影響が及び、負荷変動に対し順応する能力も失せ、混合液浮遊物質濃度MLSSも極めて薄くなる。よってBOD3,000ppmから30,000ppmからなる高濃度排水処理は不可能となる問題がある。Patent Document 2 is established in a form in which the upper part of the tank is opened when the biochemical oxygen demand BOD of 3,000 ppm is lower than the inflow wastewater. In this system, when the opening is closed, the circulatory function of microorganisms is largely lost. When the balance in the food chain is lost, the entire biological treatment is affected, the ability to adapt to load fluctuations is lost, and the mixture suspended matter concentration MLSS becomes extremely thin. Therefore, there is a problem that high-concentration waste water treatment consisting of BOD 3,000 ppm to 30,000 ppm becomes impossible.

特開2005−137969号 公報  JP-A-2005-137969 特開2003−326289号 公報  JP 2003-326289 A

文献、浄化槽の推持管理 監修:厚生省生活衛生局水道
環境部、昭和60年4月発刊
散水濾床設計諸元
容積負荷率基準 P219,BOD容積負荷 0.6kg/m.日
濾材負荷率基準 P207,BOD濾材負荷 0.1〜0.7kg/m.日
処理能力の比較資料
Literature, management management of septic tank Supervision: Ministry of Health and Welfare, Health Sanitation Bureau, Water Environment Department, published in April 1985 Sprinkling filter bed design volumetric load factor standard P219, BOD volumetric load 0.6kg / m 3 . Daily filter medium load factor standard P207, BOD filter medium load 0.1-0.7 kg / m 3 . Comparison of daily processing capacity

開口部を閉鎖した排水処理方法では高濃度の廃水液に対応する微生物群の増殖が充分でなく希薄な生物層となる。槽内の低分子化が進まず、緊殖時間を要する原生動物も少なくなり沈殿槽でのバルキング現象など環境に順応できず処理能力が悪化する傾向にある。処理能力の改善には微生物間の食物連鎖の循環は大変重要である。生物膜法に於ける一連の活動の中で微生物群を数多く必要とする原生動物や、細菌類のそれぞれの補食材とする供給源の微細な有機物Cや、有機物C合成過程で誕生する余剰有機物等を生産する時のシステム機能に影響がある為に、具体的に生物層が大変薄くなり微生物の複雑な混合培養系が成り立たず多くの相互作用ができない。少々BODの高い脂肪酸や多糖類など高分子系の廃水の場合や、負荷の変動が発生した時など微生物が順応できず、生物処理が機能しない問題が有る。In the wastewater treatment method in which the opening is closed, the microorganism group corresponding to the wastewater solution with a high concentration does not grow sufficiently, resulting in a thin biological layer. The number of protozoa that require mating time is reduced, and the processing capacity tends to deteriorate due to the lack of adaptation to the environment such as the bulking phenomenon in the sedimentation tank. Circulation of the food chain between microorganisms is very important for improving processing capacity. Protozoa that requires a large number of microorganisms in a series of activities in the biofilm method, and fine organic substances C n H m O p as sources for supplements of bacteria and organic substances C n H because of the effect on the system function when producing excess organic substances that born in m O p synthesis process, specifically complex mixed culture system of microorganisms becomes thin very biological layer can not many interactions not hold . In the case of polymer wastewater such as fatty acids and polysaccharides with a slightly higher BOD, or when fluctuations in load occur, there is a problem that the biological treatment cannot function because the microorganisms cannot adapt.

散水濾床方式を応用した従来の方式の設備は太陽光を利用した、槽の上部を開放した形態により成立している。開口部を閉鎖した場合に於いては微生物の環境機能に大きな欠落が生じ、食物連鎖のバランスが大きく崩れ、生物処理全体の機能低下により高濃度排水処理は不可能となる。高濃度で高分子など難易度の高い排水処理に於いては、生物処理に重要な相互作用による微生物間の確実な食物連鎖が前提となる。そこで開口部による人間の転落防止や、細かな水滴の飛散防止や、面積の多目的使用の為に開口部を閉鎖して太陽光を遮断する場合は、食物連鎖での一番底辺に位置する、しかも一番の緊殖数を必要とする細菌かつ微細藻類等の緊殖が得られない場合、食物連鎖の循環ができず生物膜法による生物処理が機能しない問題が有る。The conventional type of equipment that uses the sprinkling filter bed system is formed by using sunlight and opening the top of the tank. When the opening is closed, there is a large gap in the environmental function of microorganisms, the balance of the food chain is greatly disrupted, and high-concentration wastewater treatment becomes impossible due to a decline in the function of the entire biological treatment. In wastewater treatment with a high concentration and high difficulty such as a polymer, a reliable food chain between microorganisms is premised on an interaction important in biological treatment. Therefore, when the sun is blocked by closing the opening for the purpose of preventing human fall by the opening, scattering of fine water droplets, and multipurpose use of the area, it is located at the bottom of the food chain, In addition, there is a problem in that the biological treatment by the biofilm method does not work because the food chain cannot be circulated when the bacteria and microalgae that require the highest number of growth cannot be obtained.

又、従来の生物処理により処理した廃水成分は、無機物の窒素N除去が不完全で、栄養成分を残した処理水を放流することになり、河川や海洋汚染を招く原因を造っている。従来の生物処理に於いて、天然鉱石を散水濾床法及び浸漬濾床法に利用している例は多くあるが、高BOD量やノルマルヘキサンも高く、高分子の廃水の場合は閉塞作用を起こし、処理効率の高い好気性微生物の生息が難しくなると共に処理能力もおちる。これは好気性菌と、脱窒をする嫌気性菌等の異種の微生物の能力の相互作用が働かない表れである。更に負荷変動が発生した場合、処理能力がその時点で失われ悪臭を発する等の問題もある。In addition, wastewater components treated by conventional biological treatment have incomplete removal of inorganic nitrogen N 2 , and the treated water leaving the nutrient components is discharged, creating a cause of river and marine pollution. In conventional biological treatment, there are many examples where natural ore is used in the sprinkling filter bed method and submerged filter bed method, but the high BOD amount and normal hexane are also high. Wake up, it becomes difficult to inhabit aerobic microorganisms with high processing efficiency, and the processing capacity also drops. This shows that the interaction between aerobic bacteria and the ability of different microorganisms such as anaerobic bacteria to denitrify does not work. Further, when load fluctuation occurs, there is a problem that the processing capacity is lost at that time and a bad odor is generated.

従来の生物膜法による酸素供給量は低溶存効率で、送風量も過多に設定され、大気圧と水圧と吐出圧を加算した圧力で出力するモーターを長時間稼働するためエネルギーの消費量も多い。又溶存効率を考慮して高濃度BOD量の場合は処理槽の水深を5メートル程にする場合が多い、耐圧強度を得る為には構造を強化する必要がある。Oxygen supply by the conventional biofilm method is low in dissolution efficiency, excessive air flow is set, and the motor that outputs with the pressure that is the sum of atmospheric pressure, water pressure and discharge pressure is operated for a long time, so energy consumption is also large . In consideration of the dissolution efficiency, in the case of a high concentration BOD amount, the water depth of the treatment tank is often set to about 5 meters, and it is necessary to strengthen the structure in order to obtain the pressure strength.

本発明の高濃度排水処理システムは、流入する低濃度から高濃度にわたる有機性物質を、活性汚泥方式と散水濾床方式を組み合わせて低分子化をする開口部の無い廃水処理システムに於いて、発光装置で複数の槽に光を照射する装置と各槽内の微生物が発生した二酸化炭素COを再び各混合割合で曝気に利用する排出二酸化炭素CO集気管と、散水濾床槽の内部で低分子化され有機物から離れた無機質のNを速やかに大気に放つ放出通気管と、送風機により溶存酸素効果を高める溶存酸素補助器とを、有する事を特徴とした高濃度排水処理システムである。
The high-concentration wastewater treatment system of the present invention is a wastewater treatment system without an opening that reduces the molecular weight of an inflowing organic substance ranging from a low concentration to a high concentration by combining an activated sludge method and a sprinkling filter bed method. A device for irradiating light to a plurality of tanks with a light emitting device, an exhausted carbon dioxide CO 2 air collecting tube that uses again carbon dioxide CO 2 generated by microorganisms in each tank for aeration at each mixing ratio, and the inside of a sprinkling filter bed tank A high-concentration wastewater treatment system characterized by having a discharge vent pipe that quickly releases inorganic N 2 that has been reduced in molecular weight and separated from organic matter to the atmosphere, and a dissolved oxygen auxiliary device that enhances the dissolved oxygen effect by a blower. is there.

本発明の高濃度排水処理システムは、自然の光を利用できない開口部の無い処理環境で流入する高濃度の廃水液に対応する事を目的とし、人工の光を連続照射して光合成を活発化させ微生物群の安定増殖を充実させる基礎となる第一次補食材の安定供給を整える環境を提供する。従来の構造で太陽光を利用した場合、夜間の光合成は得られない、更に天候によっても左右される。そこで植物育成に必要な特有波長が400nm,500nm,600nmを選択する、照度が8,000ルックスから20,000ルックスである光を各槽の天井や壁から連続照射し安定した確実な光合成を人工的に促す。35億年前の化石より、初めて地球上に誕生した微生物としてラン藻類が記録されている。自然界に於ける生物群の構築の源は0.001mmから0.002mmの小さな微生物を第一次補食材とし、捕食した微生物は次の生物に捕食されその安定した食物連鎖が自然界の浄化構成を成立させている。本発明での生物処理は食品製造用微生物の数種を集積培養した液を濾床層に移植した後に、その微生物群を取り巻く人工的に作る事のできない多くの微生物が誕生しそれぞれの役割で活動する事を利用する。そうした自然界の微生物の総合作用で、高濃度で窒素成分の多い畜産排水の生物化学的酸素要求量BOD19,000ppmであっても、120時間滞留時間の微生物処理でBOD17ppmに浄化する能力を発揮する。有機性物質を低分子化し、酸化させ、還元させ、自然界の微生物が食物連鎖を繰り返し活動しながら、浄化する環境造りをする上で発光装置は光合成を促進させる重要な役割である。
The high-concentration wastewater treatment system of the present invention activates photosynthesis by continuously irradiating artificial light for the purpose of dealing with high-concentration wastewater liquid that flows in a treatment environment without openings that cannot use natural light. It provides an environment that provides a stable supply of primary supplementary foods that will serve as a basis for enhancing the stable growth of microorganisms. When sunlight is used in a conventional structure, nighttime photosynthesis cannot be obtained, and it also depends on the weather. Therefore, we select artificial wavelengths of 400nm, 500nm and 600nm that are necessary for plant growth, and continuously irradiate light from 8,000 lux to 20,000 lux from the ceiling and walls of each tank to produce stable and reliable photosynthesis. Promptly. Cyanobacteria are recorded as the first microorganisms born on the earth from a fossil of 3.5 billion years ago. The source of construction of organisms in nature is a small microorganism of 0.001mm to 0.002mm as a primary supplement, and the predated microorganisms are preyed on by the next organism, and its stable food chain forms a purification structure in nature. It has been established. In the biological treatment according to the present invention, after transplanting a liquid obtained by accumulating several kinds of microorganisms for food production to the filter bed layer, many microorganisms surrounding the microorganism group that cannot be artificially created are born and have their respective roles. Take advantage of activities. With such a comprehensive action of microorganisms in the natural world, even if the biochemical oxygen demand BOD is 19,000 ppm for livestock wastewater with a high concentration and a high nitrogen content, the ability to purify to 17 ppm BOD by microbial treatment for 120 hours residence time. Light emitting devices play an important role in promoting photosynthesis in reducing the molecular weight of organic substances, oxidizing them, reducing them, and creating a clean environment where natural microorganisms repeatedly act in the food chain.

本発明の高濃度排水処理システムは、流入する高濃度の廃水液に対応する微生物群は、連鎖をしながら変化する環境に於いて増殖しつつ活動をする、そうした自然界の仕組みに合致させる為の環境が提供する処理過程で微生物が発生する二酸化炭素COを、通常曝気と混合させ微細藻類の増殖環境を充実させて微細藻類を光合成により多量合成する際、同時に発生する未合成の余剰有機物を安定生産する為、微生物の活動で発生した二酸化炭素COを回収し再利用をする。水に溶けた二酸化炭素COは重炭酸イオンHCO−と変化しそれが藻類等の酵素により二酸化炭素に変換されて、水素Hと結合し新有機物CnHmOpする微細藻類が生まれる。同時に発生する未結合の余剰有機物は菌類の餌や又菌類の増殖過程に利用され、食物連鎖の重要な第一次補食材の安定した供給に繋がる。大気中の二酸化炭素濃度は0.035%と低く微生物が放出した二酸化炭素の再利用は食物連鎖の循環に効率良く働く、各槽に設けた集気装置から二酸化炭素COを回収し、BOD量に応じ送風機にて曝気量に対し集気装置で回収した量を20:1から5:1の割合で送風する。
The high-concentration wastewater treatment system of the present invention is designed to match the natural structure in which the microorganisms corresponding to the inflowing high-concentration wastewater are active while multiplying in a chain-changing environment. When carbon dioxide CO 2 generated by microorganisms in the treatment process provided by the environment is mixed with normal aeration to enrich the growth environment of microalgae to synthesize a large amount of microalgae by photosynthesis, unsynthesized surplus organic matter generated at the same time For stable production, carbon dioxide CO 2 generated by the activity of microorganisms is recovered and reused. Carbon dioxide CO 2 dissolved in water is changed to bicarbonate ion HCO 3 −, which is converted to carbon dioxide by an enzyme such as algae, and is combined with hydrogen H to produce microalgae that forms a new organic substance CnHmOp. The unbound surplus organic matter generated at the same time is used for fungal food and fungal growth processes, leading to a stable supply of important primary supplements in the food chain. The carbon dioxide concentration in the atmosphere is as low as 0.035%, and the reuse of carbon dioxide released by microorganisms works efficiently in the circulation of the food chain. Carbon dioxide CO 2 is recovered from the air collector installed in each tank, and BOD The amount collected by the air collector is blown at a ratio of 20: 1 to 5: 1 with respect to the aeration amount by a blower according to the amount.

本発明の高濃度排水処理システムに於いて、火山性の軽石状の天然鉱石と貝殻を重鎮し積み重ねた散水濾床に廃水成分の有機性物質を分解する能力を有す微生物を移植し、好気性菌あるいは嫌気性菌の持つ能力を自然界の仕組みに沿い、最大に活用する散水濾床方式を併せ持つ。散水濾床層の同一な容積内で好気性菌と通性嫌気性菌と弱嫌気性菌そして嫌気性菌が活動し、早い分解速度のもとで低分子化且つ硝化に至った硝酸NOは、通性嫌気性である脱窒細菌によって酸素Oと窒素ガスNに分解され、窒素ガスNは一部光合成に利用される、散水濾床層内部を活性化する目的で窒素ガスN集気管を設けて排出する。脱窒反応によって窒素化合物を窒素ガスまで分解すると同時に有機物除去が行われるので、余剰汚泥量を従来の0.2から0.14と極めて少量化でき、本発明のシステムに於いて重要な働きである。
In the high-concentration wastewater treatment system of the present invention, a microorganism having the ability to decompose organic substances of wastewater components is transplanted to a sprinkling filter bed in which volcanic pumice-like natural ore and shells are piled up and stacked. In addition to the ability of aerobic bacteria or anaerobic bacteria, along with the structure of nature, it also has a sprinkling filter bed system that makes the most of it. NO 3 nitrate, which has become a low molecular weight and nitrified under the fast decomposition rate, with aerobic bacteria, facultative anaerobic bacteria, weak anaerobic bacteria and anaerobic bacteria active in the same volume of the sprinkling filter bed Is decomposed into oxygen O and nitrogen gas N 2 by denitrifying bacteria that are facultative anaerobic, and nitrogen gas N 2 is partially used for photosynthesis. Nitrogen gas N is used for the purpose of activating the inside of the sprinkling filter bed layer. 2 Provide a gas collection tube and discharge. Since nitrogen compounds are decomposed to nitrogen gas by denitrification reaction and organic matter removal is performed at the same time, the amount of excess sludge can be extremely reduced from 0.2 to 0.14, which is an important function in the system of the present invention. is there.

更に散水濾床では、好気性菌と通性嫌気性菌と弱嫌気性菌そして嫌気性菌を共存させる。散水濾床槽で酸化作用や、硝化作用が行われ、汚泥減少に伴う汚泥中の硫酸塩類が嫌気性菌の硫黄塩還元細菌に還元され硫化水素HSを生成するが、本発明システムの特徴でもある光合成によって生存する硫黄酸化細菌により酸化させ無害化されると同時にメルカプタンの分解もする事で臭いを発生さないなど、好気性菌では得られない能力を有す部分で、嫌気性菌の活動役割は大きい。硫黄酸化細菌の増殖の速さは72時間に1個と大変遅い為、散水濾床槽に共存できる嫌気性菌の増殖環境は重要である。また濾材に使用する材質は多孔質の流紋岩で二酸化ケイ素SiO72%以上の天然鉱石と、炭酸カルシウム素材の貝殻を15:1から27:1の割合で混合使用して、微生物の活動に必要な炭酸カルシウムを溶脱する貝殻を混合使用する。Furthermore, in the watering filter bed, aerobic bacteria, facultative anaerobic bacteria, weak anaerobic bacteria and anaerobic bacteria coexist. Oxidation and nitrification are carried out in the sprinkling filter bed tank, and sulfates in the sludge resulting from sludge reduction are reduced to anaerobic bacterial sulfur salt-reducing bacteria to produce hydrogen sulfide H 2 S. It is an anaerobic bacterium that has an ability that cannot be obtained by aerobic bacteria, such as it does not generate odor by being oxidized and detoxified by sulfur-oxidizing bacteria that survive by photosynthesis, which is also a feature, and at the same time it decomposes mercaptans. The role of activities is great. Since the growth speed of sulfur-oxidizing bacteria is very slow, one per 72 hours, the growth environment of anaerobic bacteria that can coexist in the trickling filter is important. The material used for the filter medium is porous rhyolite, which is a mixture of natural ore with a content of 72% or more of silicon dioxide SiO 2 and shells made of calcium carbonate at a ratio of 15: 1 to 27: 1. Use shells to dissolve the calcium carbonate required for the mixing.

一方、散水濾床には食品製造用微生物である真正細菌及び菌類の数種類を適切な割合で培養した微生物群を濾材に定着させる。例えば多孔質琉紋岩の表面には好気性菌、その内側に通性嫌気性菌又、その内側に弱嫌気性菌や、嫌気性菌が住み分けをする。例えば濾材1個の大きさは250mm程の楕円形状で濾材量は有機性物質の成分とその量に応じ充填する。BOD濾材負荷率はBOD容積負荷の、22倍の13kg/m.日と大きく高濃度廃液処理に対応できる。濾材中で、微生物が必要とする炭酸塩や二酸化ケイ素と少々のマグネシウムの溶脱が発生し、これを利用できる微生物群の生息により従来の目詰まり閉塞は解決した。嫌気状態では食物連鎖の頂点に環形動物貧毛類の赤ミミズが生息し、閉塞防止の一役を担うと同時に濾床槽内部で汚泥硝化活動を行い余剰汚泥減量化に効果を上げる。On the other hand, on the sprinkling filter bed, a group of microorganisms obtained by culturing several kinds of eubacteria and fungi as microorganisms for food production at an appropriate ratio is fixed on the filter medium. For example, aerobic bacteria on the surface of porous serpentine, facultative anaerobes on the inside, weak anaerobic bacteria on the inside, and anaerobic bacteria live on the inside. For example, the size of one filter medium is an elliptical shape of about 250 mm, and the amount of the filter medium is filled according to the components of the organic substance and the amount thereof. The BOD filter media load factor is 13 times 13 kg / m 3 of the BOD volume load. It can cope with high concentration waste liquid treatment day by day. In the filter medium, leaching of carbonate and silicon dioxide required by microorganisms and a small amount of magnesium occurred, and the conventional clogging blockage was solved by the presence of microorganisms that can use this. In the anaerobic state, red earthworms of annelids are present at the top of the food chain and play a role in preventing clogging, and at the same time, sludge nitrification activities are carried out inside the filter bed tank, increasing the effect of reducing excess sludge.

本発明の高濃度排水処理システムは、効率のよい溶存酸素を供給する目的で溶存酸素補助器を使用する。本システムの溶存効果は従来の散気管だけで曝気する方法と比較して、5%から20%上昇させる事が出来る。微生物が消費する酸素量より供給酸素量が常に上回っていなければならない環境で、小さな送風機の送風量で理想的な効果を得られる。構造上の面では水圧が下がる過程で気泡玉が大きくなるものを再び小さな気泡玉にしながら湾曲した空気溜まりに気泡玉を留め、気泡玉は水膜の接触面積に触れながら滞留時間を長くする事で溶存効果を得る。よって従来の水槽深度より0.5mから1.0m浅くする事ができ構造上有利な結果が得られる。一方水圧も0.05から0.1ポイント水圧が低くなるので吐出させる送風エネルギーの削減もできる。
The high-concentration wastewater treatment system of the present invention uses a dissolved oxygen auxiliary device for the purpose of supplying efficient dissolved oxygen. The dissolved effect of this system can be increased by 5% to 20% compared to the conventional method of aeration only with a diffuser. In an environment where the amount of supplied oxygen must always exceed the amount of oxygen consumed by microorganisms, an ideal effect can be obtained with a small blower. In terms of structure, the bubble ball is retained in a curved air pocket while changing the bubble bubble that becomes larger as the water pressure is lowered into a small bubble ball, and the bubble ball makes the residence time longer while touching the contact area of the water film. Get the dissolved effect. Therefore, the depth can be made 0.5 m to 1.0 m shallower than the depth of the conventional water tank, and a structurally advantageous result can be obtained. On the other hand, since the water pressure is also reduced by 0.05 to 0.1 point, the blown energy to be discharged can be reduced.

本発明は上記のそれぞれの特徴を併せ持った設備の利用により、複雑な混合培養系からなる各微生物間の相互作用が自然界の仕組みに合った活動を充実させ、排水処理施設内部での環境に自然に順応する効果が得られる。よって生物化学的酸素要求量BOD3,000ppmから30,000ppmからなる排水や、油など高分子系の難易度の高い排水の処理を確実に施すことができる高濃度排水処理システムを実現できる。In the present invention, by utilizing the above-mentioned facilities, the interaction between microorganisms composed of complicated mixed culture systems enhances the activities that match the mechanism of the natural world, and the environment inside the wastewater treatment facility is naturally The effect of adapting to is obtained. Therefore, it is possible to realize a high-concentration wastewater treatment system capable of reliably performing treatment of wastewater consisting of biochemical oxygen demand BOD 3,000 ppm to 30,000 ppm and high-molecular wastewater such as oil.

人工的光合成環境を設ける為昼夜通しての光合成が達成できる事で、微生物による食物連鎖基礎底盤が大きくなり、全体の食物連鎖組織量が一般の微生物処理と比較しても大変多く、自然光での微生物処理に対し処理速度の向上が得られる。自然の太陽光の照射量の変動に影響されず一定した強力な光を安定供給できる事で、微生物処理基礎である食物連鎖の強力な維持が達成できる。開口部を無くして転落の危険性を除き、散水から発生する細かな水滴飛散防止で周辺の悪影響を防止し、又専有面積を別の目的で利用が可能である。更に設備施工上の問題がなければ従来深度より全体0.5mから1.0m浅く設備する事が出来る。生物処理の基本とする微生物の食物連鎖を正しく理解しそれを守るべく解決する為の手段を行ったのでそれぞれの相互の作用が充実する事で、微生物群が自ら順応する複雑な反応により負荷変動に自己対応が出来た。又、生物処理の基本が万全であるが故に以下の効果が得られた。放流基準に応じた放流水質が安定して得られ、自然の環境を守る事が出来る大きな役割を担う事ができる。活性炭等の濾過装置を必要としない。余剰汚泥の発生が従来よりも1/6以上で余剰汚泥引き抜きが大変少なく、それに準じて薬品使用量も少なくなり全体の維持管理費の大きな削減となる。処理設備から発生する硫化水素HS等の危険な成分も無く、畜産排水であっても生物処理設備からほとんど臭いが発生しない、自然の浄化機能を確実に行える様にした高濃度排水処理システムが実現できる。The ability to achieve day-and-night photosynthesis to provide an artificial photosynthetic environment increases the base of the food chain base by microorganisms, and the total amount of food chain tissue is much greater than that of general microorganism treatment. An increase in processing speed is obtained over microbial processing. The ability to stably supply a constant and powerful light without being affected by fluctuations in the amount of natural sunlight, can achieve a strong maintenance of the food chain that is the basis of microbial treatment. Eliminating the danger of falling by eliminating the opening, preventing the water from splashing finely, preventing adverse effects in the surrounding area, and the exclusive area can be used for other purposes. Furthermore, if there is no problem in equipment construction, the equipment can be installed 0.5 to 1.0 m shallower than the conventional depth. We have taken steps to correctly understand and protect the food chain of microorganisms, which is the basis of biological treatment, so that each interaction is enriched, and the load changes due to complex reactions that the microorganism group adapts to itself. I was able to deal with myself. In addition, since the basics of biological treatment are perfect, the following effects were obtained. Effluent water quality according to the effluent standards can be obtained stably and can play a major role in protecting the natural environment. No filtering device such as activated carbon is required. The generation of excess sludge is 1/6 or more than before, and excessive sludge extraction is very little, and the amount of chemicals used is reduced accordingly, which greatly reduces the overall maintenance cost. A high-concentration wastewater treatment system that does not have any dangerous components such as hydrogen sulfide H 2 S generated from treatment facilities, and that does not generate odors from biological treatment facilities even with livestock wastewater, and that can reliably perform a natural purification function. Can be realized.

又、生物処理をする容積も活性汚泥法に比べ小さい。本発明の散水濾床槽の容積に対するBOD負荷率は、前記の非特許文献P219記載のBOD容積負荷と比べた場合22倍の能力があるので、活性汚泥法より小さな容積で高濃度の難易度が高いとされている、油や澱粉など高分子系の廃水成分であっても失敗がなく、確実な廃水処理ができる。Moreover, the volume for biological treatment is also small compared to the activated sludge method. Since the BOD load factor with respect to the volume of the trickling filter bed of the present invention is 22 times higher than the BOD volume load described in Non-Patent Document P219, the degree of difficulty of high concentration with a smaller volume than the activated sludge method. Even high-molecular wastewater components such as oil and starch, which are said to be high, have no failure and can be reliably treated.

本発明の実施形態を示す生物処理システムの断面図である。It is sectional drawing of the biological treatment system which shows embodiment of this invention. 散水濾床と発光装置の断面図である。It is sectional drawing of a watering filter bed and a light-emitting device. 散水濾床槽の平面図である。It is a top view of a trickling filter bed tank. 溶存酸素補助板の側面図である。It is a side view of a dissolved oxygen auxiliary board. 溶存酸素補助板の立面図である。It is an elevation view of a dissolved oxygen auxiliary plate. 溶存酸素補助板の水膜接触面の拡大図である。It is an enlarged view of the water film contact surface of a dissolved oxygen auxiliary plate. 発光装置の設置断面図である。It is installation sectional drawing of a light-emitting device. 微生物の食物連鎖の構成図である。It is a block diagram of the food chain of microorganisms.

図1は高濃度廃液の流入から放出する迄の処理工程の流れを示すと共に処理方法を実施する為の装置を示す。FIG. 1 shows a flow of processing steps from inflow to discharge of high-concentration waste liquid and an apparatus for carrying out the processing method.

図1の9は散水濾床層を示す火山岩の一種で、二酸化ケイ素70%以上で多孔質状天然鉱石である琉紋岩等を90%から97%の割合として、貝殻を10%から3%の割合で混合した濾材を充填する。溶脱した炭酸塩又珪酸そして炭酸カルシウムを利用する。9 in FIG. 1 is a type of volcanic rock showing a sprinkling filter bed. The ratio is 90% to 97% of porphyry rocks, which are 70% or more of silicon dioxide and porous natural ore, and 10% to 3% of shells. The filter medium mixed in the ratio is filled. Leached carbonate or silicic acid and calcium carbonate are used.

高濃度廃液の処理能力を有する複数種類の食品製造用微生物を廃液成分に応じた割合で混合の集積培養し、90万匹/1mmリットルから110万匹/1mmリットルの培養液を造り濾床槽に移植し定着した後に生物処理工程が開始される。A mixture of two or more types of microorganisms for food production having the ability to process high-concentration waste liquor in a proportion corresponding to the waste liquor components, and a culture solution of 900,000 / 1 mm to 1.1 million / 1 mm liter is produced to create a filter bed tank The biological treatment process begins after transplantation and colonization.

図1の17は発光装置を示す。発光体は食物育成に働く400nm,500nm,600nmの3波長を有する放電管と、高い光反射率を有する反射板との組み合わせた器具であり、保護ケースに収納する。発光体は植物成育の光合成に必要な400nm,500nm,600nmを有する3波長帯を混合照射し、濾床上部は照度8,000ルックスから20,000ルックスで長時間照射をする。散水時に発生する細かな廃水液粒の飛散防止や、排水処理に必要とする敷地を別の用途に使用する為、又は、人間の転落事故を防ぐ為、又は、散水に発生する音を防ぐ等の理由で、開口部を設けていない排水処理施設であっても、発光装置により自然界浄化能力を発揮させる事ができ、高濃度の廃液を処理する事ができる。Reference numeral 17 in FIG. 1 denotes a light emitting device. The illuminant is a device that combines a discharge tube having three wavelengths of 400 nm, 500 nm, and 600 nm, which works for food cultivation, and a reflector having high light reflectance, and is housed in a protective case. The illuminant is mixed and irradiated with three wavelength bands having 400 nm, 500 nm, and 600 nm necessary for photosynthesis in plant growth, and the upper part of the filter bed is irradiated for a long time at an illuminance of 8,000 lux to 20,000 lux. Preventing the scattering of fine waste water droplets generated during water spraying, using the site necessary for wastewater treatment for other purposes, preventing human fall accidents, or preventing sound generated by water spraying, etc. For this reason, even in a wastewater treatment facility that does not have an opening, it is possible to exhibit the ability to purify nature by using the light emitting device, and it is possible to treat a high concentration waste liquid.

発光装置は、高濃度の廃水液を短い滞留時間で低分子化させる為であり、微生物を含めた濃度すなわち、混合液浮遊物質濃度MLSS値を高くできる。高効率の食物連鎖の循環に重要である微細藻類は一番数が多く必要とする第一次補食材となって菌類に捕食される。その補食材を光合成の働きを応用し安定供給する事が自然界浄化に於ける食物連鎖をゆるぎなくする役割であり重要である。濾材からわずかに溶脱する炭酸塩又は珪酸そして炭酸カルシウム等のミネラル分に加え微細藻類の成育に必要な波長帯の光を照射する事で、活発な光合成が働き、新しい0.001mmから0.002mmの大きさの微細藻類を多量に誕生させる環境が整い、生物処理の基本とする微生物に必要とする食物連鎖の循環を、人工的な光合成を行う事により、極めて簡単な構造で、微生物が自ら循環できる自然界浄化機能を取り入れた処理方式となる。The light emitting device is for reducing the molecular weight of a high concentration wastewater solution in a short residence time, and can increase the concentration including microorganisms, that is, the mixed solution suspended solid concentration MLSS value. Microalgae, which are important for highly efficient food chain circulation, are preyed on by fungi as the primary supplementary food that needs the largest number. It is important and important to provide a stable supply of supplementary foods by applying the action of photosynthesis to keep the food chain in the purification of nature. By irradiating light in the wavelength band necessary for the growth of microalgae in addition to minerals such as carbonate or silicic acid and calcium carbonate that are slightly leached from the filter medium, active photosynthesis works, and new 0.001mm to 0.002mm An environment that allows birth of a large amount of microalgae of the size of scientists has been prepared, and the microorganisms themselves have an extremely simple structure by artificially synthesizing the food chain circulation necessary for the microorganisms that are the basis of biological treatment. It is a treatment method that incorporates a natural purification function that can be circulated.

図1の15は排出二酸化炭素CO集気管を示す。集気管は微生物が活動工程で発する二酸化炭素COを吸引回収し、曝気装置からBOD量に応じて、集気量と曝気量との割合は1対5から1対20にして送風を行う。高濃度の廃液を生物処理で浄化するには微生物群の食物連鎖の循環が重要である。各微生物間の補食材の供給で第一次補食材は食物連鎖の始まりとなる。その補食材とする細菌領域の微細藻類等を増殖する過程で、新しい有機物誕生の大きな補助となる。大気中の二酸化炭素COの割合は0.035%と低い、通常二酸化炭素COが水に溶け重炭酸イオンHCO と変化するがこの過程で藻類等の酵素の働きで微細な二酸化炭素COとして発生し、水素Hと結合し新有機物Cとなる。これは微細藻類の誕生に大きくかかわっている。微細藻類は多くの菌類の餌として利用される。同時に発生する多量の未結合の余剰有機物は、菌類だけが利用する事ができ菌類の増殖に利用される。廃水の浄化に対し菌類の働く役割は多く、セルロースやリジンや澱粉や糖類、二糖類や多糖類等高分子の分解に優れた能力を発揮する、高濃度廃水成分の低分子化を促進させる排水処理方式となる。Reference numeral 15 in FIG. 1 denotes an exhausted carbon dioxide CO 2 air collecting tube. The air collection tube sucks and collects carbon dioxide CO 2 generated by the microorganisms in the activity process, and blows air by changing the ratio of the air collection amount and the aeration amount from 1: 5 to 1:20 according to the BOD amount from the aeration apparatus. Circulating the food chain of the microbial community is important to purify high-concentration wastewater by biological treatment. With the supply of supplementary foods between the microorganisms, the primary supplementary food becomes the beginning of the food chain. In the process of proliferating microalgae in the bacterial area as the supplementary food, it greatly assists in the birth of new organic matter. The proportion of carbon dioxide CO 2 in the atmosphere is as low as 0.035%. Usually, carbon dioxide CO 2 dissolves in water and changes to bicarbonate ion HCO 3 , but in this process fine carbon dioxide is produced by the action of enzymes such as algae. It is generated as CO 2 and combined with hydrogen H to become a new organic substance C n H m O p . This is largely related to the birth of microalgae. Microalgae are used as food for many fungi. The large amount of unbound surplus organic matter generated at the same time can be used only by fungi and is used for the growth of fungi. Wastewater that promotes the low molecular weight of high-concentration wastewater components that play an important role in the degradation of polymers such as cellulose, lysine, starch, saccharides, disaccharides, and polysaccharides. Processing method.

図1の14は放出通気管を示す。放出通気管は高密度ポリエチレン製。濾床槽の断面に対し700mmごとに設置、又、平面に対し700mm間隔で特に断面では11°勾配で配管設置をする。放出通気管の下部側に30mmの穴を多く開け、登り側の端を縦管に接合し外気に放出する。濾材は軽石状の多孔質で表面は好気性菌、通性嫌気性菌、弱嫌気性菌、嫌気性菌の順に内部に向けて異種の微生物が同一環境で生息し活動をする。中でも好気性菌の活動は最も多く、窒素を含む有機化合物である蛋白質は好気性の細菌により低分子化され、硝酸NOに至らせた後、嫌気生菌である脱窒細菌が水素と有機炭素と脱窒環境で硝酸NOを亜硝酸NOにする、更に嫌気性菌は一酸化窒素NOに分解し、更に一酸化二窒素NOに変化し、それから分離した窒素ガスNは速やかに濾材層から分別する必要がある。この工程が速やかに実行される事で、従来の生物処理より1/3から1/6の余剰汚泥量を減少させる事ができた。この様に同一環境で好気性菌から嫌気性菌の相互作用を実施できる源は、自然界浄化の基礎となる食物連鎖の最善な環境が整ったうえで達成する事である。その事によって放流水の中の窒素N量が減少する為、放流後の二次汚染防止効果が大変大きく、放出通気管の果たす効果の大きい排水処理方式となる。Reference numeral 14 in FIG. 1 denotes a discharge vent pipe. The discharge vent pipe is made of high-density polyethylene. Pipes are installed at intervals of 700 mm with respect to the cross section of the filter bed tank, and pipes are installed at an interval of 700 mm with respect to the plane, particularly with a 11 ° gradient in the cross section. Many holes of 30 mm are made on the lower side of the discharge vent pipe, and the end on the climbing side is joined to the vertical pipe to discharge to the outside air. The filter medium is pumice-like porous, and the surface has aerobic bacteria, facultative anaerobic bacteria, weak anaerobic bacteria, and anaerobic bacteria in the order of different microorganisms living in the same environment. Among these activities aerobic bacteria most often, protein is an organic compound containing nitrogen is depolymerized by bacterial aerobic, after brought to nitrate NO 3, denitrifying bacteria hydrogen and organic which is anaerobic bacteria Nitrogen NO 3 is converted to nitrous acid NO 2 in a denitrifying environment with carbon, and anaerobic bacteria are further decomposed into nitric oxide NO, further converted into dinitrogen monoxide N 2 O, and nitrogen gas N 2 separated therefrom is It is necessary to quickly separate from the filter medium layer. By carrying out this process promptly, it was possible to reduce the amount of excess sludge by 1/3 to 1/6 of the conventional biological treatment. In this way, the source of interaction between anaerobic bacteria and anaerobic bacteria in the same environment is to achieve it in the best environment of the food chain, which is the basis for natural purification. As a result, the amount of nitrogen N 2 in the discharge water is reduced, so that the secondary pollution prevention effect after the discharge is very large, and the drainage treatment system has a large effect of the discharge vent pipe.

図1の19は溶存酸素補助器を示す。従来の散気方式は床から吐出する微細な気泡を発する。水圧が下がるに反比例し気泡玉は大きくなり、上昇加速度が加わり早く液面に到達し、すぐ大気に出て効率が悪い。そこで溶存酸素補助器は底部で吐出した空気が上昇する過程で、空気が次から次に気泡粉砕板によって大きくなっては小さくされ、その繰り返しをする途中で図6の3に示す水膜接触材などが主に酸素と廃液とを接触させる役割をしており、長い時間液中に気泡玉を留め接触させる。従来の散気管と比較すると同一送風量で18%から23%増の酸素の溶存効果を得られた。高濃度の廃液に対応する微生物量は多く、その酸素の供給量は当然多く求められ、微生物の活動にもっとも適した酸素量を満たす事は重要である。更に従来の散気方法の場合は水温の変動や水深に大きく左右され、多量の曝気量を送る必要があったが本溶存酸素補助器はその必要がない。溶存酸素補助器を従来の散気管と併用する事で送風機を小さくできる。又、水槽構造物の深さを従来より0.5mから1.0m浅くしても充分な酸素量が得られるので耐圧構造上も有利になる排水処理方式となる。
Reference numeral 19 in FIG. 1 denotes a dissolved oxygen assist device. Conventional aeration systems emit fine bubbles that are discharged from the floor. Inversely proportional to the drop in water pressure, the bubble bubble becomes larger, the rising acceleration is added, the liquid level is reached quickly, and it immediately goes out to the atmosphere and is inefficient. Therefore dissolved oxygen aids in the process of air discharged at the bottom rises, air is small is larger by then bubble ball milling plate from following the water film shown in 3 8 6 in the course of the repeated The contact material or the like mainly plays a role of bringing oxygen into contact with the waste liquid, and holds the bubble balls in the liquid for a long period of time. Compared with the conventional air diffuser, the effect of dissolved oxygen was increased by 18% to 23% with the same air flow. The amount of microorganisms corresponding to a high concentration waste liquid is large, and the supply amount of oxygen is naturally required to be large. It is important to satisfy the oxygen amount most suitable for the activity of microorganisms. Furthermore, in the case of the conventional aeration method, it depends greatly on the fluctuation of the water temperature and the water depth, and it is necessary to send a large amount of aeration, but this dissolved oxygen auxiliary device is not necessary. A blower can be made small by using a dissolved oxygen auxiliary device together with a conventional diffuser. Moreover, even if the depth of the water tank structure is 0.5 m to 1.0 m shallower than the conventional depth, a sufficient amount of oxygen can be obtained.

1 原水ピット槽
2 スクリーン槽
3 流量調整槽
4 濾床層及び浸漬濾床槽
5 循環爆気槽
6 沈澱分離槽
7 殺菌槽
8 放流槽
9 散水濾床
10 ポンプピット槽
11 落下水空間
12 循環ポンプ
13 散水ポンプ
14 放出通気管
15 排出二酸化炭素CO集気管
16 散水用吐出ノズル
17 発光装置
18 散気管細用
19 溶存酸素補助器
20 散気管荒用
21 自動スクリーン
22 原水ポンプ
23 調整ポンプ
24 殺菌用薬剤筒
25 放流ポンプ兼洗浄ポンプ
26 汚泥返送管
27 点検用マンホール
28 脱窒及び還元槽であるが原水性質により29とセットで6の前に配置
29 二次爆気槽であるが原水性質により28とセットで6の前に配置
30 原水流入管
31 放流管
32 発光装置の自動洗浄管
33 部材SUS
34 部材はかまSUS
35 部材支柱SUS
36 気泡玉粉砕板SUSL
37 支柱 硬質ポリエチレン
38 水膜接触材 硬質ポリエチレン
39 重り
40 発光装置
41 発光装置保護カバー
42 換気取入れコネクター
43 換気用送風管
44 エアーフィルター
45 電源端子
46 電源用線
47 点検用蓋
48 点検用蓋
49 換気用吐出コネクター
50 保護カバー洗浄用ノズル
51 保護カバー洗浄用ノズル
52 洗浄用送水管
53 散水濾床用散水ノズル
54 散水用管
55 散水濾材
DESCRIPTION OF SYMBOLS 1 Raw water pit tank 2 Screen tank 3 Flow control tank 4 Filter bed layer and immersion filter bed tank 5 Circulation explosion tank 6 Precipitation separation tank 7 Sterilization tank 8 Discharge tank 9 Sprinkling filter bed 10 Pump pit tank 11 Falling water space 12 Circulation pump 13 Sprinkling pump 14 Discharge vent pipe 15 Discharged carbon dioxide CO 2 air collecting pipe 16 Sprinkling discharge nozzle 17 Light emitting device 18 Dispersing pipe fine 19 Dissolved oxygen auxiliary 20 Dispersing pipe roughing 21 Automatic screen 22 Raw water pump 23 Adjusting pump 24 Sterilization Drug cylinder 25 Discharge pump / washing pump 26 Sludge return pipe 27 Inspection manhole 28 Denitrification and reduction tank, but placed in front of 6 in a set with 29 due to the nature of raw water 29 Although it is a secondary explosion tank, it is 28 due to the nature of raw water Arranged in front of 6 in a set 30 Raw water inflow pipe 31 Drain pipe 32 Automatic cleaning pipe 33 of light emitting device Member SUS
34 The member is a hook SUS
35 Member support SUS
36 Bubble Ball Crush Plate SUSL
37 Strut Rigid polyethylene 38 Water film contact material Rigid polyethylene 39 Weight 40 Light-emitting device 41 Light-emitting device protective cover 42 Ventilation intake connector 43 Ventilation air duct 44 Air filter 45 Power terminal 46 Power line 47 Inspection lid 48 Inspection lid 49 Ventilation Discharge connector 50 Protective cover cleaning nozzle 51 Protective cover cleaning nozzle 52 Cleaning water pipe 53 Sprinkling filter floor sprinkling nozzle 54 Sprinkling pipe 55 Sprinkling filter medium

Claims (5)

活性汚泥方式による循環曝気槽と散水濾床方式による散水濾床槽とを組み合わせた複数の処理槽からなり、
自然光が入り込まないように開口部を無くした閉鎖型の各処理槽に対して人工光を照射する発光装置と、
循環曝気槽に設置され、槽内の微生物が排出した二酸化炭素CO を曝気に利用するために集気する排出二酸化炭素CO 集気管と、
散水濾床槽内に配設され、槽内で発生する窒素N を集気して槽外へ放出するための放出通気管と、
循環曝気槽の底面に設置され、廃液中に放出された空気の気泡を細分化し、細分化された気泡を廃液中に留め、廃液中に酸素を溶存させる溶存酸素補助器と、
循環曝気槽の底面に設置され、槽の底面付近から空気を放出する散気管と、
からなり、
溶存酸素補助器は、
上方に向かって幅が広い逆角錐台の形状をなした本体部分と、循環曝気槽の底面に立脚して本体部分を支える脚部とからなり、
本体部分には、
廃液中に放出されて本体部分を通過しながら上昇する空気の気泡を細分化する気泡玉粉砕板と、
廃液中に放出されて本体部分を通過しながら上昇する空気の気泡を留める水膜接触材と、
が設けられている
ことを特徴とする高濃度排水処理システム。
It consists of a plurality of treatment tanks that combine a circulating aeration tank with activated sludge system and a sprinkling filter bed tank with sprinkling filter bed system,
A light-emitting device that irradiates artificial light to each closed treatment tank without an opening so that natural light does not enter;
An exhausted carbon dioxide CO 2 air collection pipe that is installed in a circulating aeration tank and collects carbon dioxide CO 2 discharged by microorganisms in the tank for use in aeration ;
A discharge vent pipe disposed in the sprinkling filter bed tank for collecting nitrogen N 2 generated in the tank and releasing it outside the tank;
A dissolved oxygen auxiliary device installed on the bottom of the circulating aeration tank, which subdivides the bubbles of air released into the waste liquid, keeps the subdivided bubbles in the waste liquid, and dissolves oxygen in the waste liquid;
An air diffuser installed on the bottom of the circulating aeration tank and releasing air from the vicinity of the bottom of the tank,
Consists of
The dissolved oxygen assister
It consists of a main body part in the shape of an inverted truncated pyramid that is wide toward the top, and a leg part that stands on the bottom of the circulating aeration tank and supports the main body part,
In the body part,
A bubble ball crushing plate that subdivides the air bubbles that are released into the waste liquid and rise while passing through the main body part,
A water film contact material that is released into the waste liquid and keeps air bubbles rising while passing through the main body, and
Is provided
A high-concentration wastewater treatment system characterized by that .
活性汚泥方式による循環曝気槽と、散水濾床方式による散水濾床槽と、を組み合わせた複数の処理槽からなり、
自然光が入り込まないように開口部を無くした閉鎖型の各処理槽に対して人工光を照射する発光装置と、
循環曝気槽に設置され、槽内の微生物が排出した二酸化炭素CO を曝気に利用するために集気する排出二酸化炭素CO 集気管と、
散水濾床槽内に配設され、槽内で発生する窒素N を集気して槽外へ放出するための放出通気管と、
循環曝気槽の底面に設置され、廃液中に放出された空気の気泡を細分化し、細分化された気泡を廃液中に留め、廃液中に酸素を溶存させる溶存酸素補助器と、
循環曝気槽の底面に設置され、槽の底面付近から空気を放出する散気管と、
からなり、
前記の溶存酸素補助器は、
上方に向かって幅が広い逆角錐台の形状をなした本体部分と、循環曝気槽の底面に立脚して本体部分を支える脚部とからなり、
本体部分には、
2つの支柱(第1支柱、第2支柱)がそれぞれ列をなして交互に複数並設され、
第1支柱には、
廃液中に放出されて本体部分を通過しながら上昇する空気の気泡を細分化するための、支柱の列方向に長い、断面が逆V字型の気泡玉粉砕板が、
第2支柱には、
廃液中に放出されて本体部分を通過しながら上昇する空気の気泡を留めるための、支柱の列方向に長い、断面が下方に窪みを有する半円弧状の水膜接触材が、
それぞれ鉛直方向に複数取り付けられている
ことを特徴とする高濃度排水処理システム。
It consists of a plurality of treatment tanks that combine a circulating aeration tank with activated sludge system and a sprinkling filter bed tank with sprinkling filter bed system,
A light-emitting device that irradiates artificial light to each closed treatment tank without an opening so that natural light does not enter;
An exhausted carbon dioxide CO 2 air collection pipe that is installed in a circulating aeration tank and collects carbon dioxide CO 2 discharged by microorganisms in the tank for use in aeration ;
A discharge vent pipe disposed in the sprinkling filter bed tank for collecting nitrogen N 2 generated in the tank and releasing it outside the tank;
A dissolved oxygen auxiliary device installed on the bottom of the circulating aeration tank, which subdivides the bubbles of air released into the waste liquid, keeps the subdivided bubbles in the waste liquid, and dissolves oxygen in the waste liquid;
An air diffuser installed on the bottom of the circulating aeration tank and releasing air from the vicinity of the bottom of the tank,
Consists of
The dissolved oxygen auxiliary is
It consists of a main body part in the shape of an inverted truncated pyramid that is wide toward the top, and a leg part that stands on the bottom of the circulating aeration tank and supports the main body part,
In the body part,
Two struts (first strut, second strut) are arranged in parallel alternately in a row,
In the first column,
In order to subdivide the air bubbles that are released into the waste liquid and rise while passing through the main body part, a bubble ball crushing plate with a long V-shaped cross section in the column direction of the pillars,
In the second column,
A semicircular arc-shaped water film contact material that is long in the column direction of the pillars and has a depression in the lower part in order to keep air bubbles rising while being discharged into the waste liquid and passing through the main body part,
Multiple each mounted vertically
A high-concentration wastewater treatment system characterized by that .
前記の散気管は、
溶存酸素補助器の直下に設置される散気管細用と、
溶存酸素補助器と槽壁との間に設置される散気管荒用と、
からなる
ことを特徴とする請求項1または2に記載の高濃度排水処理システム。
The air diffuser is
For the diffuser tube installed directly under the dissolved oxygen auxiliary device,
Aeration tube ablation installed between the dissolved oxygen auxiliary device and the tank wall;
Consist of
The high-concentration waste water treatment system according to claim 1 or 2 .
前記の散水濾床槽は、
火山性で軽石状の天然鉱石と貝殻とが15:1から27:1の割合で混合された濾材が敷き詰められている
ことを特徴とする請求項1から3のいずれかの項に記載の高濃度排水処理システム。
The watering filter bed is
The filter medium is mixed with volcanic pumice-like natural ore and shells in a ratio of 15: 1 to 27: 1.
The high-concentration wastewater treatment system according to any one of claims 1 to 3 .
前記の放出通気管は、
勾配をつけて槽内に配管されており、
放出通気管の下部側には、複数の通気孔が設けられている
ことを特徴とする請求項1から4のいずれかの項に記載の高濃度排水処理システム。
The discharge vent pipe is
It is piped in the tank with a gradient,
A plurality of vent holes are provided on the lower side of the discharge vent pipe.
The high-concentration waste water treatment system according to any one of claims 1 to 4, wherein
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