KR100472972B1 - Treatment method of sewage and waste water - Google Patents

Treatment method of sewage and waste water Download PDF

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KR100472972B1
KR100472972B1 KR10-2002-0078548A KR20020078548A KR100472972B1 KR 100472972 B1 KR100472972 B1 KR 100472972B1 KR 20020078548 A KR20020078548 A KR 20020078548A KR 100472972 B1 KR100472972 B1 KR 100472972B1
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microorganisms
wastewater
sewage
stone
minerals
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KR20030009253A (en
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서희동
서영진
서영준
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서희동
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/481Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/484Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/344Biological treatment of water, waste water, or sewage characterised by the microorganisms used for digestion of mineral oil
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Activated Sludge Processes (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

본 발명은 하·폐수를 호기성생물학처리방법에 의해서 BOD, COD, 질소, 인과 같은 오염물질을 경제적으로 고도처리 할 수 있는 방법을 제시하는 것이 목적이다.An object of the present invention is to propose a method for economically and highly treating contaminants such as BOD, COD, nitrogen, and phosphorus by aerobic biological treatment of sewage and wastewater.

이를 위하여 본 발명은, 자화(磁化)자철광(磁), 미네랄(Minerals) 공급이 용이한 광물, 풀브산(Fulvic acid)함량이 많은 해양성부식산콜로이드미셀(Colloidal micelle), 영구자석 또는 전자석을 이용하여 토양미생물 중에서 하·폐수에 함유되어 있는 유기성오염물질을 물에 불용성이면서 비휘발성의 안정된 부식(전구)물질로 전환하는 부식물질 생성미생물 및 이들 미생물과 상호공생관계에 있는 미생물을 배양하여 하·폐수를 고도처리 할 수 있는 방법을 제시한다.To this end, the present invention, magnetized magnetite (磁化) Organic pollution in soil microorganisms in soil microorganisms using minerals, minerals that can be easily supplied to minerals, colloidal micelles with high content of fulvic acid, permanent magnets or electromagnets We present a method for advanced treatment of sewage and wastewater by culturing microorganisms producing corrosive substances that convert substances into insoluble and non-volatile stable corrosive materials.

특이한 사항은 하·폐수의 일반 활성오니처리방법에 비해서 처리효율이 월등히 높으면서 운전비용이 절감되며, 악취발생의 저감 등의 효과가 있기 때문에 하·폐수처리에 널리 보급될 것으로 기대된다.It is expected that it will be widely used in sewage and wastewater treatment because it has much higher treatment efficiency compared to general activated sludge treatment method of sewage and wastewater, and it has the effect of reducing odor.

Description

하·폐수처리방법{Treatment method of sewage and waste water}Treatment method of sewage and waste water

본 발명은 부식물질 중에서 풀브산(Fulvic acid) 함량이 높은 해양성 동·식물이 규조류와 광물질이 함께 퇴적된 해양성부식산콜로이드미셀(Colloidal micelle)에 자화된 자철광분말을 혼합하여 제조된 펠렛트(Pellet)와 자화된 자철광괴, 수중에서 가용성미네랄 성분이 다량 함유된 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(Pumice), 흑요석(黑曜石), 각섬석(角閃石), 천매암(千枚岩). 맥반석(飯石), 감람석(橄欖石), 송지암(松脂岩), 진주석(珠石), 호실석(戶室石), 거정석(巨晶石)과 같은 광물질과 영구자석이나 전자석을 이용하여 토양미생물 중에서 하·폐수에 함유되어 있는 유기성오염물질을 물에 불용성이면서 비휘발성의 안정된 부식(전구)물질로 전환하는 부식물질 생성미생물 및 이들 미생물과 상호공생관계에 있는 미생물을 배양하여 하·폐수를 고도처리 할 수 있는 방법에 관한 것이다.The present invention is a pellet prepared by mixing magnetized magnetite powder in marine corrosive acid colloidal micelle in which marine animals and plants having high Fulvic acid content are deposited with diatoms and minerals. ), Magnetized magnetite mass, rhyolite or dacite-like pumice, obsidian, hornblende and chalcedony rock containing a large amount of soluble minerals in water ). Elvan Stone ( Stone, olive stone, songji-am, pearl stone Inorganic contaminants contained in sewage and wastewater among soil microorganisms are insoluble and nonvolatile in soil microorganisms using minerals such as stone, stone stone, and giant stone, and permanent or electromagnets. The present invention relates to a method for highly treating sewage and wastewater by culturing microorganisms that generate corrosive substances and converting them into stable corrosive (bulb) materials.

일본 특허공보 평()5-66199호에서는 부식토(Humus soil)를 펠렛트형태로 가공한 것과 유문암 또는 대사이드질의 부석을 충전(充塡)한 생물반응기를 배양조에 설치하고, 유기성물질을 함유한 폐수의 처리에서 부식토 및 부석 중에서 4,3산화철의 함량이 낮거나 산화환원전위(ORP ; Oxidation Reduction Potential)값이 낮은 폐수의 경우에는 처리효율이 향상되지 못하는 문제점이 있다.Japanese Patent Publication In the case of 5-66199, humic soil was processed into pellets, and bioreactors filled with rhyolite or pumice pumice were installed in the culture tank, and humus soil was treated in the treatment of wastewater containing organic substances. And in the case of wastewater having a low content of iron 4, trioxide, or a low Oxidation Reduction Potential (ORP) value among pumice stones, there is a problem that treatment efficiency is not improved.

본 발명은 상기와 같은 문제점을 해소하기 위해 배양조 및 폭기조에서 부식물질 생성미생물 및 상호공생관계에 있는 미생물의 최적의 환경조건으로 유지하여 하·폐수의 처리를 고도처리 할 수 있는 방법을 제공하는 데 본 발명의 목적이 있는 것이다.The present invention is to provide a method that can be highly treated treatment of sewage and waste water by maintaining the optimum environmental conditions of the corrosive substances generated microorganisms and microorganisms in mutual symbiosis in the culture tank and aeration tank to solve the above problems. It is an object of the present invention.

이와 같은 목적을 달성하기 위한 본 발명은, 부식토는 가능한 풀브산 함량이 높은 해양성부식산콜로이드미셀을 산성으로 조정하여 풀브산을 유리(遊離)의 상태로 유도한 다음 착자(着磁)된 자철광분말과 수중에서 가용성미네랄성분이 용출하기 쉬운 광물질의 분말을 혼합하여 숙성한 다음에 가공한 펠렛트, 착자된 자철광, 수중에서 가용성미네랄성분이 용출하기 쉬운 광물과 연구자석이나 전자석을 이용하여 부식물질 생성미생물 및 상호공생관계에 있는 미생물을 배양하여 하·폐수 중 유기성오염물질을 경제적으로 고도처리 한다.In order to achieve the above object, the present invention provides a caustic earth with a high content of fulvic acid, and adjusts the acidic corrosive colloid micelle to acid to induce fulvic acid to a free state and then magnetize magnetite powder. Aging is made by mixing and pulverizing mineral powders in which soluble minerals are easily eluted in water and water, and then using processed pellets, magnetized magnetite, minerals in which soluble minerals are easily eluted in water and using research magnets or electromagnets. By cultivating microorganisms and microorganisms with mutual symbiosis, it is economically advanced treatment of organic pollutants in sewage and wastewater.

본 발명에서 사용하는 산성의 해양성부식산콜로이드미셀(Colloidal micelle)은 해양성 동·식물 및 규조류가 산성화산회토나 광물질이 혼합 퇴적하여 생성된 부식토(Humus soil)로서 화산회토나 광물질 중 활성화된 알루미나(Al2O3), 시리카(SiO2) 및 기타 미네랄 성분이 물과 가수분반응에 의해서 수소이온(H+)이 방출되어 강산성의 토양으로 되면서 풀브산(Fulvic acid)이 유리(遊離)의 상태로 존재하여 각종 미네랄성분은 킬레이트(Chelate)성 미네랄착염형태로 존재한다.The acidic marine corrosive colloidal micelle used in the present invention is a humus soil in which marine animals, plants and diatoms are mixed and deposited with acidic ash or minerals, and activated alumina in volcanic ash or minerals (Al 2). O 3 ), silica (SiO 2 ) and other minerals are released as hydrogen ions (H + ) by water and hydrolysis reaction to form a strongly acidic soil, and fulvic acid is present in the free state. Therefore, various mineral components exist in the form of chelate mineral complex salts.

미네랄 공급이 충분하였을 때 활발한 대사활동을 하는 바칠루스 마이코이데스(Bacillus mycoides), 아스페르길루스 니거(Aspergillus niger), 페니실륨 그라우컴(Penicillium glaucum), 소랑 세루로섬(Sorangium cellulosum), 악티노미세스 그로비오포러스 로세어스(Actinomyces globioporus roseus)와 같은 방선균과 같이 폴리페놀(Polyphenol)성 대사산물을 배설하여 유기물질을 부식물질(腐植物質)로 전환하는 부식화미생물과 이들 미생물과 상호공생관계에 있는 미생물이 활발한 활동을 하게되며, 반면에 이들 미생물과 상호길항관계에 있는 병원성미생물과 부패 및 변패성(혐기성)미생물의 생육은 억제된다.Bacillus mycoides, Aspergillus niger, Penicillium glaucum, and Sour, which have active metabolism when mineral supply is sufficient Corrosion that converts organic substances into corrosive substances by excretion of polyphenolic metabolites such as actinomycetes, such as Sorangium cellulosum and Actinomyces globioporus roseus Microorganisms that interact with symbiotic organisms and these microorganisms are active, while growth of pathogenic microorganisms and rot and decaying (anaerobic) microorganisms which are antagonistic with these microorganisms is suppressed.

특히 자성을 띈 자철광과 풀브산이 반응하여 생성된 킬레이트성풀브산철염(Chelatic iron fulvate) 성분이 다량 함유된 부식산콜로이드미셀의 경우에는 이들 미생물대사활동이 더욱더 활발하게 된다.In particular, in the case of colloidal micelles containing a large amount of chelate iron fulvate, which is formed by the reaction of magnetite magnetite with fulvic acid, these microbial metabolism activities become more active.

또한, 해양성부식산콜로이드미셀 중에는 미생물의 생육에 필요한 생리적 활성물질, 성장촉진물질 및 기타 활성효소 등이 다량 함유되어 있어 이들 미생물의 생육을 촉진하는 효과가 있다.In addition, the marine corrosive colloid micelles contain a large amount of physiologically active substances, growth accelerators and other active enzymes necessary for the growth of microorganisms, thereby promoting the growth of these microorganisms.

따라서 해양성부식산콜로이드미셀에 염산(HCl)이나 황산(H2SO4)와 같은 광산(酸)을 주입하여 pH를 2.3이하로 조정하여 풀브산(Fulvic acid)을 유리(遊離)의 상태로 유도한 다음 자속밀도(磁束密度)가 가능한 400G(Gauss)이상 착자(着磁)된 자철광(磁)을 40∼60㎛정도 분쇄한 분말을 4∼10wt%을 혼합하고, 각섬석(角閃石), 감람석(槪欖石), 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(浮石)과 같이 수중에서 미네랄(Minerals)성분을 용이하게 용출하는 조암광물(造岩物)을 단독 또는 2종류 이상 혼합하여 40∼60㎛정도로 분쇄한 분말을 유기물/무기물의 비가 0.8∼1.2의 범위로 혼합한 후 1개월 이상 숙성하여 킬레이트성풀브산철염(Chelatic iron fulvate) 및 기타 유기산미네랄착염 형태로 전환한 다음 펠렛트(Pellet) 형태로 성형가공하여 건조한 것을 사용한다.Therefore, marine corrosive acid colloid micelles (such as hydrochloric acid (HCl) or sulfuric acid (H 2 SO 4 )) 을) by injecting Fulvic acid into the free state by adjusting the pH to 2.3 or less, and then magnetizing magnetite with a magnetization of 400 G or more (Gauss) capable of magnetic flux density.磁 ) 4 to 10 wt% of powder ground to 40 to 60 µm, mixed with hornblende, olivine, rhyolite, or large-sided pumice stone. Crude minerals that easily elute minerals in water. Chelated iron fulvate and other organic acids after mixing powders alone or in combination of two or more kinds, pulverized to about 40 to 60 탆, and mixed at an organic / inorganic ratio in the range of 0.8 to 1.2, for at least one month. After conversion to mineral complex salt form, it is molded into pellet form and dried.

자성자철광은 물(유체)이 자성자철광(자성체)의 자장(磁場) 사이를 흐르면 자기유체역학(MHD ; Magneto-Hydro-Dynamics)전압이 발생하면서 약전해질인 물은 전기분해 되면서 ╋전위측에서는 (활성)산소가 발생하며, ━전위측에서는 수소를 발생하며, 활성산소는 유기물질, 부패성물질과 같은 환원성물질을 산화하여 안정화되며, 또한, 물이 자철광의 자계(磁界)를 통과하면서 전자의 파동(波動)에 의해서 물분자의 집단체(集團 ; Cluster)가 미세화(微細化)되면서 표면장력(表面張力)이 적어져 침투력(浸透力)이 향상되어 용해력이 향상되며, 탈취효율도 향상되고, 미생물의 세포막 투과율이 향상되어 미생물의 대사활동을 활발하게 한다.Magnetic magnetite generates magnetic fluid dynamics (MHD) when water (fluid) flows between the magnetic fields of magnetic magnetite (magnetic material), and water, which is a weak electrolyte, is electrolyzed. ) Oxygen is generated, -The hydrogen is generated at the potential side, and the active oxygen is stabilized by oxidizing reducing substances such as organic substances and perishable substances, and also the wave of electrons as water passes through the magnetic field of magnetite. Group of water molecules ; As the microstructure becomes smaller, surface tension is reduced, so that penetration force is improved, solubility is improved, deodorization efficiency is improved, and cell membrane permeability of microorganism is improved, so that metabolic activity of microorganism is enhanced. Let's do it.

그리고, 광물은 풍화작용에 의해 각종 미네랄(Minerals) 성분의 용출이 용이한 각섬석(角閃石), 감람석(橄欖石), 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(浮石), 흑운모(黑雲母), 흑요석(黑曜石), 진주암(珠岩), 송지암(松脂岩), 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(Pumice), 호실석(戶室石), 거정석(巨晶石), 천매암(千枚岩), 맥반석(飯石)과 같은 광물을 1종류 이상을 혼합하여 사용한다.In addition, minerals are hornblende, olivine, rhyolite or luteite-like pumice and biotite, which are easy to elute various minerals by weathering. Black stone, obsidian, pearl rock Stone, Songji rock, Rhyolite or Dacite, Pumice, Lake stone, Giant stone, Cheonmae rock ), Elvan Use at least one kind of mineral such as 石.

이하 도면을 중심으로 본 발명의 내용을 상세히 설명하면 다음과 같다.Hereinafter, the contents of the present invention will be described in detail with reference to the drawings.

하·폐수의 호기성생물학처리의 경우에 도 1에서와 같이 일반활성오니처리공정에 침전조의 반송오니 일부를 해양성부식산콜로이드미셀에 자속밀도가 400G이상 자화된 자절광 분말과 가용성미네랄성분이 다량 함유된 조암광물의 분말을 혼합하여 펠렛트(Pellet) 형태로 성형 가공한 것과 자속밀도가 400G이상 착자된 자철광괴(磁塊)와 전술한 풍화작용에 의해 각종 미네랄(Minerals) 성분의 용출이 용이한 광물괴(物塊) 등의 충전물(3)을 충전한 생물반응기(Bio-Reactor ; 2)를 설치한 배양조(1)로 보내어 킬레이트성미네랄착염 및 기타 활성효소 등을 공급받아 폴리페놀(Polyphenol)성 대사산물을 배설하여 하·폐수에 함유된 유기성오염물질을 물에 불용성이면서 비휘발성인 부식물질(腐植物質)로 전환하는 부식화미생물과 이들 미생물과 상호공생관계에 있는 미생물을 배양하여 폭기조로 반송하므로서 전체 처리시스템(System)이 부식화반응(Humification)에 의해서 유기성오염물질이 부식물질로 전환되어 수질이 정화되는 환경분위기로 전환된다.In the case of aerobic biological treatment of sewage and wastewater, as shown in Fig. 1, part of the return sludge of the sedimentation tank in the general activated sludge treatment process contains a large amount of magneto-optic powder and soluble mineral component magnetized with a magnetic flux density of 400G or higher A mixture of powdered coarse mineral powder was formed into pellets and magnetized ingots magnetized with a magnetic flux density of 400 G or more. Iv) and mineral masses which are easy to elute various minerals by the above-mentioned weathering action. Polyphenol metabolism is sent to the culture tank (1) equipped with a bio-reactor (2) filled with a filler (3), etc., and supplied with chelating mineral complex salts and other active enzymes. By excreting products, cultivating corrosive microorganisms that convert organic pollutants contained in sewage and wastewater into insoluble and nonvolatile corrosive substances in water, and microorganisms in mutual symbiosis with these microorganisms, and returning them to the aeration tank. The entire system is converted to an environmental atmosphere in which organic pollutants are converted to corrosive substances by the corrosion, and the water quality is purified.

이때 미생물의 배양효율을 보다 향상하기 위해서 배양조순환펄프(Pump ; 4)의 토출측에 자속밀도가 10,000G이상 착자된 영구자석(永久磁石)이나 전자석(電磁石)을 설치하여 배양조(1)의 배양액을 이들 자석의 자계(磁界)을 순환시켜 자화된 물을 공급하며, 또한 소독산화조의 산화수를 공급하여 산화환원전위(ORP ; Oxidation Reduction Potential)값을 +250∼+350mV 범위로 조정한다.At this time, in order to further improve the microbial culture efficiency, a permanent magnet or electromagnet having a magnetic flux density of 10,000 G or more magnetized on the discharge side of the culture tank circulating pulp 4 is used to culture the culture medium of the culture tank 1. By circulating the magnetic field of these magnets to supply magnetized water, and supplying the oxidized water of the disinfection oxidizing tank, the Oxidation Reduction Potential (ORP) value is adjusted in the range of +250 to +350 mV.

배양조(1)에 생물반응기(2)의 설치는 도 3에서와 같이 배양조(1)내부에 설치하거나 도 4에서와 같이 배양조(1) 외부에 설치하는 2가지 경우가 있다.There are two cases in which the bioreactor 2 is installed in the culture tank 1 in the culture tank 1 as shown in FIG. 3 or outside the culture tank 1 as shown in FIG. 4.

하·폐수가 집수조에 유입되면 침전조의 반송오니 일부를 공급받아 송풍기로부터 공기를 주입하여 폭기를 하면 전술한 유기물질을 물에 불용성이면서 비휘발성인 부식물질로 전환하는 폴리페놀성 대사산물을 배설하는 부식화미생물 및 이들 미생물과 상호공생관계에 있는 미생물들에 의해서 1차 분해 및 부식화 반응이 일러나면서 악취발생이 저감되며, 이를 폭기조로 이송하여 공기를 주입하여 폭기를 하면 하·폐수 중 유기성오염물질은 물에 불용성 물질이면서 비휘발성인 부식(전구)물질 및 미생물균체로 전환하여 침전조로 보낸다.When sewage and wastewater enter the collection tank, a part of the return sludge of the sedimentation tank is supplied to inject air from the blower to aeration to excrete the polyphenolic metabolite that converts the aforementioned organic substances into insoluble and nonvolatile corrosive substances. Corrosive microorganisms and microorganisms having mutual symbiosis with these microorganisms lead to the first decomposition and erosion reactions, leading to the reduction of odors.They are transferred to an aeration tank to infuse air and aeration to induce organic pollution in sewage and wastewater. The material is converted to a non-volatile corrosive (bulb) material and microbial cells that are insoluble in water and sent to the settling tank.

침전조에 유입되면 물에 불용성인 부식(전구)물질 및 미생물균체와 같은 고형물질은 침전조 하부에 침전되고, 고형물질이 분리된 청등수는 침전조 상부로 익류되어 소독산화공정으로 보낸다.When it enters the sedimentation tank, solid materials such as corrosive (bulb) materials and microbial cells insoluble in the water are precipitated at the bottom of the sedimentation tank, and the blue water separated from the solid matter is fed to the sedimentation tank and sent to the disinfection oxidation process.

침전조에 침전된 고형물(오니)은 종균용으로 집수조 및 폭기조로 반송하며, 일부는 배양조로 보내어 전술한 내용에서와 같이 부식화미생물 및 이들 미생물과 상호공생관계에 있는 미생물들을 배양 및 활성화하여 폭기조로 반송하면 처리공정 전체시스템이 이들 미생물에 의해서 처리되는 환경분위로 전환되며, 그리고 잉여오니는 오니처리공정(탈수처리 등)으로 보내어 처리한다.Solids (sludge) precipitated in the sedimentation tank are returned to the collection tank and the aeration tank for spawning, and some are sent to the culture tank to cultivate and activate the corrosive microorganisms and microorganisms having mutual symbiosis with these microorganisms as aeration tanks. When returned, the entire processing process system is converted to an environmental atmosphere treated by these microorganisms, and the surplus sludge is sent to a sludge treatment process (such as dehydration treatment).

침전조에서 익류된 청등수는 소독산화처리공정으로 보내어 산화제를 주입하여 미처리된 유기오염물질을 산화분해하면서 미생물을 멸균처리 후 방류하며, 소독산화공정의 산화수 일부는 원활한 부식화반응이 일러나게 하기 위해서 폭기조, 배양조, 집수조 등에 산화환원전위(ORP) 값을 +250∼+350mV범위로 조정하기 위해서 반송한다.Cheongdeung water from the sedimentation tank is sent to the disinfection oxidation treatment process to inject oxidants to oxidize untreated organic pollutants and sterilize the microorganisms and then discharge them. In order to adjust the ORP value in the range of +250 to +350 mV, it is returned to the aeration tank, the culture tank, and the collection tank.

그리고, 시운전초기나 비정상운전이 되는 경우에는 해양성부식산콜로이드미셀에 자속밀도가 200G이상 착자된 자철광분말을 4∼10wt%정도 혼합하고, 천매암, 각섬석, 감람석, 유문암 또는 대사이드질의 부석과 같은 광물질분말을 유기물/무기물의 비가 0.8∼1.2의 비율로 혼합하여 1개월 이상 숙성한 것을 안정제로 집수조, 폭기조, 배양조 등에 0.00006∼0.06wt% 범위로 주입하여 빠른 시간에 정상상태의 운전이 되도록 한다.In case of initial trial run or abnormal operation, magnetite powder mixed with marine corrosive acid colloid micelle magnetized with magnetic flux density of 200G or more is mixed with 4-10 wt%, and minerals such as natural stone, hornblende, olivine, rhyolite or pavement stone. The powder is mixed at an organic / inorganic ratio at a ratio of 0.8 to 1.2 and aged for at least one month, and injected into the sump, aeration tank, and culture tank in the range of 0.00006 to 0.06 wt% to stabilize the operation in a short time.

축산폐수, 식품공장배출폐수, 분뇨와 같은 고농도 유기성폐수의 경우에는 도 2에서와 같이 2단 또는 이 이상의 다단생물학처리공정에 의해서 처리하며, 이때 부식화미생물 및 이들 미생물과 상호공생관계에 있는 미생물의 배양공정(조)은 전술한 도 1의 공정과 동일하며, 배양조는 가능한 각단에 각각 설치한다.In case of high concentration organic wastewater such as livestock wastewater, food factory discharge wastewater, and manure, it is treated by two or more stages of multistage biological treatment process as shown in FIG. 2, wherein the corrosive microorganisms and microorganisms having mutual symbiosis with these microorganisms The culturing step (tank) is the same as the above-described process of Figure 1, the cultivation tank is installed at each stage possible.

[실시 예1]Example 1

아파트단지에서 배출되는 생활오폐수 600㎥/일(평균)을 일반 활성오니공법에 의해서 처리하는 곳에 유기물질을 물에 불용성이면서 비휘발성인 부식물질로 전환하는 부식화미생물과 이들 미생물과 상호공생관계에 있는 미생물을 배양하는 도 3과 같은 배양공정을 도 1의 공정에 적용하여, 침전조에서 반송하는 오니를 유입유량의 10% 정도를 배양조예 주입하고, 1.2일정도의 체류시간으로 폭기를 하면서 미생물의 배양 및 활성화를 한 후 폭기조에 공급하여 운전한 결과 처리수의 수질은 표 1의 내용에서와 같이 고도로 처리되었으며, 또한 전력소모량이 60%정도 절감되면서 처리장내 악취발생이 월등히 저감되었다.Corrosion-induced microorganisms that convert organic substances into insoluble and nonvolatile corrosive substances in water where 600m3 / day (average) of household wastewater discharged from apartment complexes are treated by the general activated sludge process The cultivation process as shown in Fig. 3 for culturing the microorganisms is applied to the process of Fig. 1, and about 10% of the inflow flow rate is injected into the culture tank with sludge returned from the settling tank, and the aeration time is maintained for 1.2 days. After cultivation and activation, the aeration tank was operated and the water quality of the treated water was highly treated as shown in Table 1, and the power consumption was reduced by 60%, resulting in a significant reduction in odor in the treatment plant.

〔실시예 2〕EXAMPLE 2

슬러리(Slurry)돈사에서 배출되는 축산분뇨를 탈수공정에서 고형분을 탈수 처리 한 후 탈수여액 12∼15㎥/일을 3단 활성오니공정에 의해서 처리하는 곳에 1단과 2단에 도2에서와 같이 도 3과 같은 배양공정을 설치하여 처리한 결과 표 2의 내용에서와 같이 처리효율이 월등히 향상되었으며, 특히 처리장에서 악취발생은 월등히 감소되었다.The livestock manure discharged from the slurry pig sludge is dehydrated in the dehydration process, and then dehydrated filtrate 12-15m 3 / day is treated in a three-stage activated sludge process in the first and second stages as shown in FIG. As a result of installing and incubating the culture process as shown in Table 3, the treatment efficiency was greatly improved as shown in Table 2, and in particular, the odor was greatly reduced in the treatment plant.

이상에서 전술한 바와 같이 본 발명에서는 부식화반응에 의한 하·폐수처리에서 부식화반응에 의한 처리는 처리효율이 일반활성오처리에 비해서 월등히 높으면서 악취발생이 저감되며, 또한 운전비용이 저렴하기 때문에 앞으로 하·폐수의 생물학처리에 널리 보급될 것으로 전망된다As described above, in the present invention, the treatment by the corrosion reaction in the sewage and wastewater treatment due to the corrosion reaction has a significantly higher treatment efficiency than the general active waste treatment, and thus, the generation of odor is reduced and the operating cost is low. It is expected to be widely used for biological treatment of sewage and wastewater in the future.

도 1은 하·폐수처리공정도1 is a wastewater treatment process diagram

도 2는 고농도 폐수처리공정도2 is a high concentration wastewater treatment process chart

도 3은 생물반응기가 배양조 내부에 설치된 미생물배양공정도Figure 3 is a microbial culture process diagram of the bioreactor installed inside the culture tank

도 4는 생물반응기가 배양조 외부에 설치된 미생물배양공정도Figure 4 is a microbial culture process diagram of the bioreactor installed outside the culture tank

[도면의 주요부분에 대한 부호의 설명][Explanation of symbols on the main parts of the drawings]

1 : 배양조 2 : 생물반응기(Bio-Reactor)1: culture tank 2: bio-reactor

3 : 해양성부식산콜로이드미셀 4 : 배양조순환펌프(Pump)3: marine corrosion acid colloid micelle 4: culture tank circulation pump (Pump)

(Colloidal micelle)펠렛트(Pellet),     (Colloidal micelle) Pellet,

자성자철광, 광물질 충전물    Magnetite, Mineral Filler

5 : 영구자석 또는 전자석 6 : 정류기5: permanent magnet or electromagnet 6: rectifier

Claims (3)

하·폐수의 호기성생물학처리 공정에서 침전조의 반송오니 일부를 해양성부식산콜로이드미셀에 자속밀도(磁束密度)가 400G이상 자화된 자절광분말과 가용성미네랄성분이 다량 함유된 각섬석(角閃石), 감람석(橄欖石), 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(浮石), 흑운모(黑雲母), 흑요석(黑曜石), 진주암(珠岩), 송지암(松脂岩), 유문암(流紋岩) 또는 대사이드(Dacite)질의 부석(Pumice), 호실석(戶室石), 거정석(巨晶石), 천매암(千枚岩). 맥반석(飯石)의 분말을 1종류 이상 혼합하여 펠렛트(Pellet)로 성형 가공한 것과 자화된 자철광괴(磁塊)와 미네랄(Minerals)성분의 용출이 용이한 광물괴(物塊)의 충전물(3)이 충전된 생물반응기(Bio-Reactor ; 2)를 설치한 배양조(1)로 보내어 킬레이트성미네랄착염 및 기타활성효소를 공급받아 폴리페놀(Polyphenol)성대사산물을 배설하여 하·폐수에 함유된 유기성오염물질을 물에 불용성이면서 비휘발성인 부식물질(腐植物質)로 전환하는 부식화미생물과 이들 미생물과 상호공생관계에 있는 미생물을 배양하면서 보다 활성화된 미생물을 배양하기 위해서 배양조(1)의 순환펌프(Pump ; 4)의 토출측에 자속밀도가 10,000G이상 착자된 영구자석(永久磁石)이나 전자석(電磁石)을 설치하여 배양액을 순환하여 자화된 물을 공급하면서 소독산화공정의 산화수를 공급하여 산화환원전위(ORP) 값을 +250∼+350mV범위로 조정하면서 부식화미생물과 이들 미생물과 상호공생관계에 있는 미생물을 배양 및 활성화하여 폭기조로 반송하므로 전체 처리시스템(System)이 부식화반응(Humification)에 의해서 유기성오염물질을 처리하는 방법.Part of the sludge returned from the sedimentation tank in the aerobic biological treatment process of sewage and wastewater, agglomerates and olivines containing a large amount of self-aggregated light powder and soluble minerals with magnetic flux density of 400 G or more Pumice, Rhyolite or Dacite-like pumice, biotite, obsidian, pearlite Stone, Songji rock, Rhyolite or Dacite, Pumice, Lake stone, Giant stone, Cheonmae rock ). Elvan Stone ( One or more kinds of powders of granite are mixed and molded into pellets and magnetized magnetite ingots Iv) mineral masses that are easy to elute and minerals It is sent to a culture tank (1) equipped with a bio-reactor (2) filled with a filler (3) of the product and supplied with chelating mineral complex salts and other active enzymes to obtain polyphenolic metabolites. Cultivation of more active microorganisms by cultivating corrosive microorganisms that excrete and convert organic pollutants contained in sewage and wastewater into insoluble and nonvolatile corrosive substances in water and microorganisms in mutual symbiosis with these microorganisms To this end, a permanent magnet or electromagnet having a magnetic flux density of 10,000 G or more magnetized on the discharge side of the circulating pump 4 of the culture tank 1 is circulated through the culture medium to supply magnetized water. Oxidation water in the disinfection oxidation process is supplied to adjust the redox potential (ORP) to the range of +250 to +350 mV, cultivating and activating corrosive microorganisms and microorganisms that are mutually related to these microorganisms and returning them to the aeration tank. Since the method by which the entire process system (System) processing the organic pollutants by the corrosion reaction (Humification). 제 1항에 있어서, 고농도 유기성폐수(축산폐수, 식품공장 배출폐수, 분뇨)의 경우에는 2단 이상의 다단생물학처리공정에 배양공정을 각단에 설치하여 처리하는 방법.The method according to claim 1, wherein in the case of high concentration organic wastewater (livestock wastewater, food factory discharge wastewater, manure), two or more stages of multistage biological treatment processes are installed at each stage and treated. 제 1항에 있어서, 시운전초기나 비정상운전이 되는 경우에는 해양성부식산콜로이드미셀에 자속밀도가 200G이상 착자된 자철광분말을 4∼10wt% 혼합하고, 천매암, 각섬석, 감람석, 유문암 또는 대사이드질의 부석을 1종류이상 분말을 유기물/무기물의 비가 0.8∼1.2의 비율로 혼합하여 1개월 이상 숙성한 안정제를 집수조, 폭기조와 배양조에 0.00006∼0.06wt% 범위로 주입하여 빠른 시간에 정상상태의 운전이 되도록 하는 방법.The method according to claim 1, wherein in the case of initial trial run or abnormal operation, 4-10 wt% of magnetite powder having magnetic flux density of 200 G or more is mixed with marine corrosive acid colloid micelles, and natural stone, hornblende, olivine, rhyolite or pavement stone. One or more kinds of powders are mixed at an organic / inorganic ratio ratio of 0.8 to 1.2, and a stabilizer matured for at least one month is injected into the sump, the aeration tank, and the culture tank in the range of 0.00006 to 0.06wt%, so as to operate in a steady state quickly. How to.
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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6135826A (en) * 1984-07-27 1986-02-20 Enzaimu Kogyo Kk Removal of malodor by activated humic substance
JPH0531490A (en) * 1991-08-02 1993-02-09 Ebara Jitsugyo Kk Biological treatment of organic sewage
JPH11128977A (en) * 1997-11-04 1999-05-18 Tomio Fuchigami Night soil treatment apparatus
KR20010088932A (en) * 2001-08-08 2001-09-29 서영준 Method for sewage and wastewater treated use of the activated humic substance
KR20020024253A (en) * 2002-02-09 2002-03-29 서영진 Treatment method for organic wastewater
KR100331725B1 (en) * 1994-12-27 2002-10-31 미나또상교가부시끼가이샤 Deodorizing composition and deodorizing resin composition containing iron(ⅱ) compound
KR20020094946A (en) * 2002-11-25 2002-12-18 서희동 Manufacturing and using method of stabilizer for sewage and waste water biological treatment

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6135826A (en) * 1984-07-27 1986-02-20 Enzaimu Kogyo Kk Removal of malodor by activated humic substance
JPH0531490A (en) * 1991-08-02 1993-02-09 Ebara Jitsugyo Kk Biological treatment of organic sewage
KR100331725B1 (en) * 1994-12-27 2002-10-31 미나또상교가부시끼가이샤 Deodorizing composition and deodorizing resin composition containing iron(ⅱ) compound
JPH11128977A (en) * 1997-11-04 1999-05-18 Tomio Fuchigami Night soil treatment apparatus
KR20010088932A (en) * 2001-08-08 2001-09-29 서영준 Method for sewage and wastewater treated use of the activated humic substance
KR20020024253A (en) * 2002-02-09 2002-03-29 서영진 Treatment method for organic wastewater
KR20020094946A (en) * 2002-11-25 2002-12-18 서희동 Manufacturing and using method of stabilizer for sewage and waste water biological treatment

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