KR100405268B1 - The contactive filter for purification of the polluted water and waste water - Google Patents

The contactive filter for purification of the polluted water and waste water Download PDF

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KR100405268B1
KR100405268B1 KR10-2001-0034588A KR20010034588A KR100405268B1 KR 100405268 B1 KR100405268 B1 KR 100405268B1 KR 20010034588 A KR20010034588 A KR 20010034588A KR 100405268 B1 KR100405268 B1 KR 100405268B1
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wastewater
chitosan
purification
contact
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KR20020096249A (en
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송정호
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신성메디아 주식회사
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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
    • C02F3/10Packings; Fillings; Grids
    • C02F3/105Characterized by the chemical composition
    • C02F3/106Carbonaceous materials
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/06Aerobic processes using submerged filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/10Packings; Fillings; Grids
    • C02F3/105Characterized by the chemical composition
    • C02F3/107Inorganic materials, e.g. sand, silicates
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/10Packings; Fillings; Grids
    • C02F3/109Characterized by the shape
    • 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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection
    • 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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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Water Treatment By Sorption (AREA)
  • Physical Water Treatments (AREA)

Abstract

본 발명은 오,폐수 정화용 접촉 여재에 관한 것으로, 좀 더 구체적으로는 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조하고, 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 잔량의 BOD 및 SS를 제거함과 동시에 소독과 탈취 및 살균의 효과가 우수하도록 할 수 있었다.The present invention relates to a contact medium for filthy and wastewater purification, and more specifically, it is composed of 2 to 37% by weight of chitosan, 5 to 40% by weight of bioceramic, 3 to 38% by weight of activated carbon, and 55 to 90% by weight of naphthalene. Each powder is mixed and pressed at a pressure of about 1 kg / cm 2 to produce a ball shape, and 0.5 to about 1000 kg / hour of primary treated water flowing into the disinfection tank in a wastewater treatment facility by contact oxidation method. In the amount of 2% by weight to remove the residual amount of BOD and SS at the same time it was able to have excellent effects of disinfection, deodorization and sterilization.

Description

오,폐수 정화용 접촉 여재{The contactive filter for purification of the polluted water and waste water}Contact filter for purification of the polluted water and waste water

본 발명은 정화조의 소독조 내로 유입되는 오,폐수를 접촉산화방식을 사용하여 1차 처리된 오폐수를 간편하게 정화 처리를 할 수 있도록 하는 오,폐수 정화용 접촉 여재에 관한 것으로, 좀 더 구체적으로는 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조된 것으로, 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 잔량의 BOD 및 SS를 제거함과 동시에 소독과 탈취 및 살균의 효과를 갖도록 하는 오,폐수 정화용 접촉 여재에 관한 것이다.The present invention relates to a contact medium for filthy and effluent purification, which enables a clarification treatment of filthy water that has been primarily treated using contact oxidation for filthy and effluent introduced into a disinfection tank of a septic tank. More specifically, chitosan 2 -37% by weight, bioceramic 5-40% by weight, activated carbon 3-38% by weight and naphthalene 55-90% by weight, each powder is mixed and pressed to a pressure of about 1kg / ㎠ to make a ball shape In the wastewater treatment facility by contact oxidation method, 0.5 ~ 2% by weight of the primary treated water flowing into the disinfection tank is removed in the amount of 0.5 to 2% by weight to remove the residual amount of BOD and SS. The present invention relates to a contact medium for wastewater purification which has an effect of deodorization and sterilization.

일반적으로 미생물을 이용한 오,페수 처리방법으로는 활성슬러지법과 접촉산화법으로 대별되며, 활성슬러지법은 미생물을 부유 성장시키는 방법이지만 접촉산화법은 여재에 미생물을 부착시켜 증식시킨다는 점에서 차이가 있을 뿐이다.In general, the sewage treatment method using microorganisms is roughly classified into activated sludge method and catalytic oxidation method. The activated sludge method is a method of floating growth of microorganisms, but the catalytic oxidation method differs only in that microorganisms are attached to and propagated by media.

특히, 접촉산화법은 도 1에 도시된 바와 같은 처리 공정에 의하여 행하여 지는 것으로, 처리의 고도화 및 비용의 감소를 목적으로 개발된 처리방법의 하나로, 여재의 표면에 미생물막을 형성시켜 폐수와의 접촉을 반복시킴으로써 생물학적 산화와 물리적 여과를 통하여 폐수중의 오염물을 제거하는 공법이며, 반응조내의 미생물 농도가 여재의 비표면적에 비례하기 때문에 미생물 농도를 높게 유지할 수 있어 높은 부하에서도 처리가 가능하고, 단일 반응조내에서 산화 반응과 여과 작용이 동시에 일어나므로 부유물이 적은 깨끗한 처리수를 얻을 수 있을 뿐만 아니라 유지관리가 간편하며 유지비용이 적게 소요된다는 장점이 있다.In particular, the catalytic oxidation method is performed by a treatment process as shown in FIG. 1, and is one of the treatment methods developed for the purpose of enhancing the treatment and reducing the cost, and forming a microbial film on the surface of the media to contact the wastewater. It is a method that removes contaminants in waste water through biological oxidation and physical filtration by repeating, and because the concentration of microorganisms in the reaction vessel is proportional to the specific surface area of the media, the concentration of microorganisms can be kept high, so it can be processed under high load. At the same time, the oxidation reaction and the filtration action occur at the same time, so that it is possible to obtain clean treated water with less suspended matter, as well as easy maintenance and low maintenance cost.

또한, 활성슬러지법은 처리 효율이 아주 우수하고, 고농도 폐수 처리에 적합하며, MLSS의 조정이 가능하므로 많이 사용되고 있지만 슬러지 발생이 과다하고, 유지 관리가 어려우며, 전문기술이 필요하고 설비가 복잡하다는 문제가 있는 바, 접촉산화법과 활성슬러지법은 일장일단이 있어 주위 환경에 따라 적절히 선택하여 사용하면 바람직한 효과를 얻을 수 있다.In addition, activated sludge method has been widely used because it has excellent treatment efficiency, is suitable for high concentration wastewater treatment, and can adjust MLSS, but there is excessive sludge generation, maintenance is difficult, requires professional skills and complex facilities. Since the catalytic oxidation method and the activated sludge method have one piece, it is possible to obtain a desirable effect if it is properly selected and used according to the surrounding environment.

그러나, 접촉산화법과 활성슬러지법을 이용하여 오,폐수를 처리하는 경우에 방류수에 부유 미생물의 농도가 높고, 미립자의 함량이 높아 퇴적물의 생성 원인이 되기도 하며, 고부하의 오,폐수가 유입될 경우 잔존 유기물에 의한 BOD 및 SS가 높은 경향이 있고, 처리수의 냄새 제거가 완전하게 이루어지지 않는 등의 문제점이 있어 1차 처리수를 소독조에서 소독하여 방류하고 있다.However, when the wastewater is treated using catalytic oxidation and activated sludge, high concentrations of suspended microorganisms in the effluent and high particulate content can cause sediment formation. BOD and SS due to the remaining organic matters tend to be high, and there is a problem that the odor of the treated water is not completely removed, and the first treated water is disinfected in the disinfection tank and discharged.

소독조에서 소독을 행할 경우 일반적으로는 무기 화학약품, 특히 휘발성이 강한 화학약품(예를 들어, 나프탈렌)을 사용하여 방류시 휘발이 이루어지도록 하는 방법을 사용하고 있으나 살균 효과는 상승되는 반면에 살균된 미생물 자체가 또 다른 오염원의 역할을 할 뿐만 아니라 다른 기능을 수행하지 못하여 효율이 좋지 못한 단점이 있었다.In case of disinfection in the sterilization tank, in general, inorganic chemicals, especially highly volatile chemicals (eg, naphthalene) are used to volatilize during discharge. The microorganism itself not only serves as another pollutant, but also has a disadvantage of poor efficiency because it does not perform other functions.

따라서, 본 발명의 목적은 미생물을 이용한 오,폐수 처리방법에 있어서 잔량의 BOD 및 SS를 제거함과 동시에 소독조에서의 소독에 의하여 살균된 미생물 자체가 또 다른 오염원으로 작용하지 않으며, 소독과 탈취 및 살균의 효과를 갖도록 하는 오,폐수 정화용 접촉 여재를 제공하는 데 있다.Accordingly, an object of the present invention is to remove the residual amount of BOD and SS in the wastewater treatment method using microorganisms and at the same time, microorganisms sterilized by disinfection in a disinfection tank do not act as another contaminant, disinfection and deodorization and sterilization. It is to provide a contact medium for wastewater purification to have the effect of.

본 발명의 다른 목적은 상기 목적의 오,폐수 정화용 접촉 여재를 용이하게제조할 수 있는 방법을 제공하는 데 있다.It is another object of the present invention to provide a method for easily manufacturing a contact medium for purifying wastewater and wastewater for the above purpose.

본 발명의 또 다른 목적은 상기 목적의 오,폐수 정화용 접촉 여재를 이용하여 오,폐수를 정화하는 방법을 제공하는 데 있다.Still another object of the present invention is to provide a method for purifying wastewater by using contact media for purifying wastewater of the above purpose.

상기 목적들 뿐만 아니라 용이하게 표출되는 또 다른 목적을 달성하기 위하여 본 발명에서는 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조하고, 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 잔량의 BOD 및 SS를 제거함과 동시에 소독과 탈취 및 살균의 효과가 우수하도록 할 수 있었다.In order to achieve the above object as well as another easily expressed object in the present invention is composed of 2 to 37% by weight of chitosan, 5 to 40% by weight of bioceramic, 3 to 38% by weight of activated carbon and 55 to 90% by weight of naphthalene , Each powder is mixed and pressed to a pressure of about 1㎏ / ㎠ to produce a ball shape, 0.5 to 1000kg / hour of the primary treatment water flowing into the disinfection tank in the wastewater treatment facility by the contact oxidation method In the amount of ~ 2% by weight to remove the residual amount of BOD and SS at the same time it was possible to have excellent effects of disinfection, deodorization and sterilization.

도 1은 본 발명의 접촉 여재가 적용되는 오수정화시설의 개략적인 처리 계통도이고,1 is a schematic treatment flow diagram of a sewage purification plant to which the contact media of the present invention is applied;

도 2는 본 발명의 접촉 여재를 X선 형광분석기로 분석한 결과를 나타내는 그래프이다.2 is a graph showing the results of analyzing the contact media of the present invention with an X-ray fluorescence spectrometer.

* 도면의 주요 부분에 대한 부호의 설명* Explanation of symbols for the main parts of the drawings

1. 스크린조 2. 예비 수로1. Screen bath 2. Spare channel

3. 유량 조정조 4. 유량 조정 탱크3. Flow Adjustment Tank 4. Flow Adjustment Tank

5. 제1접촉폭기조 6. 제2접촉폭기조5. The first contact aeration tank 6. The second contact aeration tank

7. 침전조 8. 소포조7. Sedimentation tank 8. Defoaming tank

9. 소독조 10. 방류조9. Disinfection tank 10. Discharge tank

11. 오니 농축 저류조11. Sludge Concentration Storage Tank

본 발명을 첨부 도면에 의거하여 좀 더 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings.

본 발명에 따른 오,폐수 정화용 접촉 여재는 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조된 것을 특징으로 한다.The wastewater purification contact medium according to the present invention comprises 2 to 37% by weight of chitosan, 5 to 40% by weight of bioceramic, 3 to 38% by weight of activated carbon, and 55 to 90% by weight of naphthalene. It is characterized in that it is manufactured in a ball shape by pressing at a pressure of about kg / ㎠.

또한 본 발명에 따른 오,폐수 정화 방법은 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조된 오,폐수 정화용 접촉 여재를 0.5 ∼ 2중량%의 양으로 투입하고 소독조를 가동하는 것을 특징으로 한다.In addition, the wastewater purification method according to the present invention is 2 to 37% by weight of chitosan and 5 to 40% by weight of bioceramic to 1000 kg / hour of primary treatment water flowing into the disinfection tank in the wastewater treatment facility by the catalytic oxidation method. %, Activated carbon 3 to 38% by weight and naphthalene 55 to 90% by weight, 0.5 to 2 of the contact medium for filthy and wastewater purification, prepared in a ball shape by mixing the respective powders and pressing them at a pressure of about 1 kg / cm 2. It is characterized in that the amount is added in the amount of weight and operating the sterilization tank.

키토산은 갑각류(게, 가재, 새우, 오징어뼈) 등에서 출출되어지고, N-아세틸글루코사민(N-acetylglucosamine)과 글루코사민(Glucosamine)이라는 당 3,000 - 5,000개가 연결되어 만들어진 고분자 다당으로서, 본 발명에서는 항균효과, 중금속의 제거 효과 및 흡착 효과를 나타내도록 첨가되어진다.Chitosan is a polymer polysaccharide which is extracted from crustaceans (crabs, crayfish, shrimp, squid bones) and the like, and is composed of 3,000 to 5,000 sugars called N-acetylglucosamine and glucosamine. It is added to exhibit heavy metal removal effect and adsorption effect.

키토산에 의한 항균작용은 매카니즘이 정확히 밝혀지지는 않았지만, 키토산이 유기산과 함께 존재할 때 아미노기가 양이온을 나타냄으로서 키토산의 아미노기의 양이온이 박테리아 체표면의 단백질중의 카르복실기(음이온)와 결합하여 균체표면을 스태킹(stacking)하여 균이 분열되지 못하고 영양분을 흡수하지 못하여 균의 증식이 억제되는 것으로 추정된다.Although the mechanism of antibacterial action by chitosan is not known precisely, when chitosan is present with organic acid, amino group shows cation, so cation of amino group of chitosan binds to carboxyl group (anion) in protein of bacterial body surface. It is estimated that the growth of the bacteria is inhibited by stacking and the bacteria cannot be divided and absorb the nutrients.

또한, 키토산이 아미노기(NH2 +)라는 플러스(+) 이온을 가지고 있기 때문에 중금속, 독극물질(중금속이나 독극물질은 마이너스(-) 이온을 가진다.)과 결합하므로서 1차 처리수에 잔존하거나 미처리된 중금속과 독극물질이 제거된다.In addition, since chitosan has a positive (+) ion called the amino group (NH 2 + ), it is combined with heavy metals and toxic substances (heavy metals or toxic substances have negative (-) ions) and remains or is not treated in the primary treatment water. Heavy metals and poisons are removed.

특히, 키토산은 글루코사민 한개당 한개의 아미노기와 두개의 수산기가 존재하고 있어 중금속에 대한 킬레이트 이온교환 수지로서의 효과를 발현하며, 전이 금속류에 대한 친화성이 높은 효과가 있고, 경우에 따라서는 가교 키토산 또는 그라프트-공중합 키토산을 사용하므로서 오,폐수 처리 효율을 향상시킬 수 있다.In particular, chitosan has one amino group and two hydroxyl groups per glucosamine, thus exhibiting its effect as a chelate ion exchange resin for heavy metals, and having a high affinity for transition metals, and in some cases crosslinking chitosan or graphene. By using T-copolymer chitosan, the efficiency of wastewater treatment can be improved.

즉, 키토산 비드(키토산 용액을 알카리 용액에 적하하여 제조한 것)에 황화합물을 도입함으로서 산성용액에서도 금속의 흡착이 가능한 표면적이 넓은 키토산 비드를 제조하여 중금속 또는 귀금속에 대하여 선택적 흡착능력을 향상시킬 수 있으며, 말레산(Maleic acid), 푸마르산(Fumaric acid), 이타콘산(Itaconic acid)과 같은 알켄디오익 에시드(Alkenedioic acid)에 의하여 그라프트-공중합시킨 키토산 비드는 금속이온 제거능을 더욱 향상시킬 수 있다.In other words, by introducing sulfur compounds into chitosan beads (prepared by dropping chitosan solution into alkaline solution), chitosan beads having a large surface area that can adsorb metals even in acidic solutions can be improved in selective adsorption to heavy or precious metals. In addition, chitosan beads graft-copolymerized with alkenedioic acid, such as maleic acid, fumaric acid, and itaconic acid, may further improve metal ion removal ability. .

뿐만 아니라, 키토산은 분자량이 큰 중금속과 쉽게 결합하고 분자가 큰 물질을 흡착하므로서 오,폐수 처리의 효율을 증가시킨다.In addition, chitosan easily combines with heavy metals of high molecular weight and adsorbs large molecules, thereby increasing the efficiency of wastewater treatment.

키토산, 특히 키토산 비드는 비드 크기가 작을수록 금속 제거 효율이 우수하고, 오,폐수가 통과하는 유속이 느릴수록 금속제거 효율이 증가되며, 본 발명에서는 2 ∼ 37중량%를 사용하는 것이 효과적이었다.Chitosan, in particular chitosan beads, the smaller the bead size, the better the metal removal efficiency, the slower the flow rate of wastewater, the metal removal efficiency is increased, in the present invention it was effective to use 2 to 37% by weight.

키토산의 사용량이 2중량% 미만일 경우에는 첨가 효과가 미약한 단점이 있고, 37중량%를 초과할 경우에는 첨가 상승효과가 미약하여 경제적이지 못한 문제점이 있으며, 키토산 자체가 고가이기 때문에 최적의 효과를 발현시킬 수 있는 비율을 반복실험을 통하여 정할 수 있다.If the amount of chitosan used is less than 2% by weight, there is a disadvantage in that the addition effect is weak, and if it exceeds 37% by weight, there is a problem in that it is not economical due to the weak addition synergy effect, and because chitosan itself is expensive, it has an optimal effect. The ratio that can be expressed can be determined through repeated experiments.

바이오 세라믹은 바이오 세라믹은 무기물질을 사용하는 산화물(Oxide), 질화물(Nitride), 탄화물(Carbide) 등의 재료로 일반적으로 금속재료, 유기재료에 비하여 내식성, 내열성, 내마모성 등이 매우 크며, 전자기적 기능, 기계적 기능, 광학적 기능, 생체적 기능 등의 다양한 기능을 갖고, 본 발명에서는 항균작용, 환경호르몬 등 각종 유해물질의 광산화분해, 지속적인 세균 및 곰팡이 살균과 악취 제거 작용, 휘발성 물질의 흡착과 분해, 원적외선 방사로 인한 물의 활성화, 중금속 제거 및 흡착, 소독조 내의 스케일 제거 역할을 위하여 첨가되는 것으로, 상기와 같은 작용은 바이오 세라믹에서 이미 밝혀진 바 있으나, 본원 발명에서와 같이 소독조에 첨가되는 접촉 여재의 성분으로는 거의 사용된 바 없으며, 사용량은 5 ∼ 40중량%가 효과적이었다.Bio ceramics are materials such as oxides, nitrides and carbides that use inorganic materials. Generally, bio ceramics have much higher corrosion resistance, heat resistance, and abrasion resistance than metal materials and organic materials. It has various functions such as function, mechanical function, optical function, biological function, etc. In the present invention, antibacterial action, photooxidative decomposition of various harmful substances such as environmental hormones, continuous bacteria and mold sterilization and odor removal action, adsorption of volatile substances and It is added for the role of decomposition, activation of water due to far-infrared radiation, heavy metal removal and adsorption, descaling in the sterilization tank, the above action has already been found in the bio-ceramic, but the contact media added to the disinfection tank as in the present invention It was hardly used as a component, and the use amount was 5 to 40 weight% effectively.

바이오 세라믹의 사용량이 5중량% 미만일 경우에는 첨가 효과가 미약하고, 40중량%를 초과할 경우에는 첨가 상승효과가 미약하여 경제적이지 못한 문제점이 있다.When the amount of the bio-ceramic is less than 5% by weight, the effect of addition is weak, and when it exceeds 40% by weight, there is a problem in that it is not economical because the addition synergy is weak.

활성탄은 탄소로 구성된 물질(목재, 야자각, 갈탄, 역청탄 등의 탄화물)을 고도의 활성화에 의하여 미세공이 잘 발달되도록 한 것으로서 활성화 과정에서 발달된 무수한 미세공간의 통로로 연결된 넓은 내부 표면적을 갖게 되어 탈색, 탈취, 용제 회수 유해가스제거 등 다양한 용도로 사용되며, 본 발명에서는 잔존 유기물의 여과, 탈색, 탈취 등의 효과를 나타낸다.Activated carbon is a material that is made of carbon (carbide such as wood, coconut shell, lignite, bituminous coal) so that the micropores are well developed by high activation, and has a large internal surface area connected to the path of countless microspaces developed during the activation process. Used for various purposes such as decolorization, deodorization, removal of solvent recovery harmful gas, and the present invention exhibits effects such as filtration, decolorization, deodorization of remaining organic matter.

활성탄의 사용량은 3 ∼ 38중량%를 사용하는 것이 바람직하며, 활성탄의 사용량이 3중량% 미만일 경우에는 잔존 유기물의 여과, 1차 처리된 처리수의 BOD와 SS제거 효율 저하, 탈색, 탈취 효과가 미약한 단점이 있고, 38%를 초과할 경우에는 활성탄이 탈리되는 경향이 높아 활성탄의 사용으로 인한 효과의 내구성이 저하되며, 활성탄 자체가 오염원으로 작용하는 등의 문제점이 있다.It is preferable to use 3 to 38% by weight of activated carbon, and when the amount of activated carbon is less than 3% by weight, the remaining organic material is filtered, the BOD and SS removal efficiency of the first treated water is decreased, decolorization, and deodorizing effect are achieved. There is a weak disadvantage, if the excess exceeds 38% activated carbon tends to be desorbed, the durability of the effect due to the use of activated carbon is reduced, there is a problem such that the activated carbon itself acts as a pollution source.

나프탈렌은 분자식 C10H8의 방향족 탄화수소, 무색의 휘발성을 지닌 결정으로서, 분자량 128, 녹는점 80.3℃, 끓는점 217.97℃, 비중이 0.975(25℃)이며, 상온에서도 승화되기 쉽다.Naphthalene is an aromatic hydrocarbon having a molecular formula C 10 H 8 , a colorless volatile crystal having a molecular weight of 128, a melting point of 80.3 ° C, a boiling point of 217.97 ° C, and a specific gravity of 0.975 (25 ° C), and are easily sublimed even at room temperature.

나프탈렌은 소독조에서 1차 처리된 처리수의 소독을 위하여 통상적으로 사용되지만 장기간 사용에 의하여 나프탈렌이 휘발되므로 자주 나프탈렌을 첨가하여야 하는 문제점이 있을 뿐만 아니라 단순히 소독이라는 효과만이 발현되는 데 반하여 본원 발명에서는 소독을 물론 다른 성분들과의 압착에 의하여 내구성을 향상시킬 수 잇는 효과가 잇는 것이다.Naphthalene is commonly used for disinfection of treated water firstly treated in a disinfection tank. However, since naphthalene is volatilized by long-term use, naphthalene is frequently added, but only the effect of disinfection is expressed. Disinfection, as well as compression with other ingredients can improve the durability.

나프탈렌의 사용량은 55 ∼ 90중량%이 바람직하고, 사용량이 55중량% 미만일 경우에는 초기의 소독 효과가 저하되는 단점이 있으며, 90중량%를 초과할 경우에는 다른 성분들에 의하여 발현되는 효과가 저하됨과 동시에 나프탈렌이 쉽게 승화되거나 오,폐수에 함유되어 있는 유기물에 의하여 분해되어 내구성이 현저히 저하되는 문제점이 있다.The use amount of naphthalene is preferably 55 to 90% by weight, and when the amount is less than 55% by weight, the initial disinfecting effect is lowered. When the amount is more than 90% by weight, the effect expressed by other components is reduced. At the same time, there is a problem that naphthalene is easily sublimed or decomposed by organic substances contained in wastewater and wastewater, thereby significantly reducing durability.

상기에서 설명된 성분들의 분말 특히, 키토산은 비드 형태의 것을 사용하여 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 본 발명의 오,폐수 정화용 접촉 여재를 제조한다.The powder of the above-described components, in particular chitosan, is mixed using a bead form and pressed at a pressure of about 1 kg / cm 2 to produce the contact media for the wastewater purification of the present invention in a ball shape.

압착시 압력은 특별히 한정되는 것은 아니며, 1㎏/㎠ 정도의 압력으로 압착하는 것이 제조되는 본 발명의 오,폐수 정화용 접촉 여재의 내구성이 우수하고, 접촉 여재에서 발현되는 효과 또한 우수하며, 사용 용도, 유입되는 오,폐수 종류 및 성상 등에 따라 다양한 압력으로 압착하여 강도가 다른 제품을 얻을 수 있다.The pressure at the time of compression is not particularly limited, and the pressure of the contact medium for filthy and wastewater purification of the present invention produced by pressing at a pressure of about 1 kg / cm 2 is excellent, and the effect expressed in the contact medium is also excellent. It can be compressed to various pressures according to the type of wastewater, wastewater, and properties to obtain products with different strengths.

또한, 본 발명의 오,폐수 정화용 접촉 여재는 볼형상 뿐만 아니라 다양한 형상으로 제조가 가능하며, 이는 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자라면 용이하게 유추할 수 있는 것이다.In addition, the contact media for the waste water purification of the present invention can be manufactured in a variety of shapes as well as the ball shape, which can be easily inferred by those skilled in the art.

본 발명의 오,폐수 정화용 접촉 여재를 X선 형광 분석기를 이용하여 분석한 결과, 도 2에 도시된 바와 같이 Ca, K, Fe, Si, S, Sr, Ti, Cl 등 다양한 성분으로 구성되어 있음을 알 수 있었다.As a result of analyzing the contact media for filthy water and wastewater purification of the present invention using an X-ray fluorescence analyzer, as shown in FIG. 2, Ca, K, Fe, Si, S, Sr, Ti, Cl, etc. are composed of various components. And it was found.

상기와 같이 제조된 본 발명의 오,폐수 정화용 접촉 여재는 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 사용되어 진다.The contact media for filthy and wastewater purification of the present invention prepared as described above is added in an amount of 0.5 to 2% by weight relative to 1000 kg / hour of primary treated water flowing into the disinfection tank in the filthy and effluent treatment facility by the catalytic oxidation method. It is used.

사용량이 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5중량% 미만일 경우에는 처리 효율이 현저히 저하되고, 2중량%를 초과할 경우에는 첨가 상승효과가 미약하여 경제적이지 못하다.If the amount is less than 0.5% by weight relative to the 1000kg / hour of the first treatment water flowing into the disinfection tank, the treatment efficiency is significantly lowered, and when the amount exceeds 2% by weight, the synergistic effect of the addition is weak and not economical.

다음의 실시예는 본 발명을 좀 더 상세히 설명하는 것이지만, 본 발명의 범주를 한정하는 것은 아니다.The following examples illustrate the invention in more detail, but do not limit the scope of the invention.

실시예 1Example 1

키토산 용액을 알카리 용액(5% NaOH)에 적하하여 제조한 키토산 비드 5중량%, 바이오세라믹 분말(대성세라믹연구소 제품, 상품명(SUPER CERAMIC BALL)) 2중량%, 활성탄 분말 7중량%, 60% 농도의 나프탈렌 분말 70중량%를 혼합하여 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 본 발명의 오,폐수 정화용 접촉 여재를 제조한다.Chitosan bead was added dropwise to alkaline solution (5% NaOH), 5% by weight of chitosan beads, 2% by weight of bioceramic powder (Daesung Ceramic Institute, trade name (SUPER CERAMIC BALL)), 7% by weight of activated carbon powder, 60% concentration 70 wt% of naphthalene powder was mixed and pressed at a pressure of about 1 kg / cm 2 to prepare a contact medium for filthy wastewater purification according to the present invention in a ball shape.

그 다음에 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 1중량%의 양으로 오,폐수 정화용 접촉 여재를 투입하여 정화하였다.Subsequently, in the amount of 1% by weight based on 1000 kg / hour of primary treatment water flowing into the disinfection tank, the wastewater purification contact filter was purified.

비교예로 나프탈렌(러브스타(주)제품)만을 이용하여 오,폐수 정화를 행하고 그 시험 결과를 비교한 결과, 본 발명의 오,폐수 정화용 접촉 여재를 사용시 BOD, SS, 중금속 함량, 휘발성 물질의 함량 등이 현저히 저하되어 효과가 우수함을 알 수 있었다.As a comparative example, the wastewater was purified using only naphthalene (lovestar Co., Ltd.) and the test results were compared. When the contact media for wastewater purification of the present invention were used, BOD, SS, heavy metal content, volatile substances It was found that the effect and the like is significantly lowered.

상술한 바와 같이 본 발명에서는 키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠ 정도의 압력으로 압착하여 볼형상으로 제조하고, 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 잔량의 BOD 및 SS를 제거함과 동시에 소독과 탈취 및 살균의 효과가 우수하도록 할 수 있었다.As described above, the present invention comprises 2 to 37% by weight of chitosan, 5 to 40% by weight of bioceramic, 3 to 38% by weight of activated carbon, and 55 to 90% by weight of naphthalene. It is manufactured in the shape of a ball by pressing at a pressure of 0, and the residual amount of BOD is added in the amount of 0.5 to 2% by weight based on 1000 kg / hour of primary treatment water flowing into the disinfection tank in the wastewater treatment facility by contact oxidation method. And while removing the SS was able to excellent effect of disinfection, deodorization and sterilization.

Claims (3)

키토산 2 ∼ 37중량%, 바이오세라믹 5 ∼ 40중량%, 활성탄 3 ∼ 38중량% 및 나프탈렌 55 ∼ 90중량%로 구성되며, 각각의 분말을 혼합하고 1㎏/㎠의 압력으로 압착하여 볼형상으로 제조된 것을 특징으로 하는 오,폐수 정화용 접촉 여재.It consists of 2 to 37% by weight of chitosan, 5 to 40% by weight of bioceramic, 3 to 38% by weight of activated carbon, and 55 to 90% by weight of naphthalene. Each powder is mixed and compressed into a ball shape at a pressure of 1 kg / cm 2. Contact media for filthy and wastewater purification, characterized in that manufactured. 제 1 항에 있어서, 키토산은 키토산 용액을 알카리 용액에 적하하여 제조한 비드임을 특징으로 하는 오,폐수 정화용 접촉 여재.According to claim 1, Chitosan is a contact medium for wastewater purification, characterized in that the bead prepared by dropping the chitosan solution to the alkaline solution. 제 1 항 또는 제 2항 기재의 오,폐수 정화용 접촉 여재를 접촉산화방식에 의한 오,폐수처리시설에 있어서 소독조에 유입되는 1차 처리수 1000㎏/시간에 대하여 0.5 ∼ 2중량%의 양으로 투입하여 사용함을 특징으로 하는 오,폐수 정화 방법.The contact medium for purifying wastewater and wastewater according to claim 1 or 2, in an amount of 0.5 to 2% by weight relative to 1000 kg / hour of primary treated water flowing into the disinfection tank in the wastewater treatment facility by the catalytic oxidation method. Wastewater purification method characterized in that it is put into use.
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JPH0760277A (en) * 1993-08-31 1995-03-07 Netsuren:Kk Hollow ceramic ball for cleaning waste water
US5543056A (en) * 1994-06-29 1996-08-06 Massachusetts Institute Of Technology Method of drinking water treatment with natural cationic polymers
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JP2000301186A (en) * 1999-04-16 2000-10-31 Senju Pharmaceut Co Ltd Water cleaning filter medium
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0760277A (en) * 1993-08-31 1995-03-07 Netsuren:Kk Hollow ceramic ball for cleaning waste water
US5543056A (en) * 1994-06-29 1996-08-06 Massachusetts Institute Of Technology Method of drinking water treatment with natural cationic polymers
KR20000055546A (en) * 1999-02-08 2000-09-05 김동남 Apparatus for treating sewage or waste water with aquatic microorganism
JP2000301186A (en) * 1999-04-16 2000-10-31 Senju Pharmaceut Co Ltd Water cleaning filter medium
KR20010044062A (en) * 2000-07-11 2001-06-05 고재경 The manufacturing method of ceramic ball for water treatment
KR200229205Y1 (en) * 2001-01-22 2001-07-03 신영길 Accelerating agents for nitrification and denitrification, adsorption, decomposition and oxidation removal of organic substances and odors, hardly decomposable substances in waste water

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