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KR100443691B1 - Waste Water Treatment System Using Chitosan Media - Google Patents

Waste Water Treatment System Using Chitosan Media Download PDF

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KR100443691B1
KR100443691B1 KR10-2001-0071549A KR20010071549A KR100443691B1 KR 100443691 B1 KR100443691 B1 KR 100443691B1 KR 20010071549 A KR20010071549 A KR 20010071549A KR 100443691 B1 KR100443691 B1 KR 100443691B1
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tank
chitosan
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wastewater treatment
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이승현
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주식회사 고도엔바
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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
    • C02F3/108Immobilising gels, polymers or the like
    • 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
    • C02F3/005Combined electrochemical biological processes
    • 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
    • C02F3/104Granular carriers
    • 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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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Organic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Biodiversity & Conservation Biology (AREA)
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  • General Chemical & Material Sciences (AREA)
  • Molecular Biology (AREA)
  • Electrochemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

본 발명은 접촉산화법에 의한 오폐수 처리장치에 관한 것으로, 본 발명에서는 침사조, 스크린조, 부패조, 유량조정조, 접촉폭기조, 침전조 및 살균방류조를 포함하는 접촉산화법에 의한 오폐수 처리장치에 있어서, 상기 접촉폭기조는 키토산이 코팅된 키토산접촉재로 충진되고 4조 이상으로 구분되어 1차조에서는 박테리아섬모, 2차조에서는 광합성 세균, 3차조 이후에서는 조류에 의해 오폐수에 포함된 유기물이 흡착분해될 수 있도록 이루어진 것을 특징으로 하는 키토산 접촉재를 이용한 오폐수 처리장치가 제공된다. 본 발명에 따라 구성된 접촉폭기조는 키토산 접촉재상에 생물막 및 오염물의 부착이 원활히 이루어지고 이로 인한 오염물의 소화분해가 촉진욈으로써 우수한 오폐수 처리 효과를 갖게되며, 또한 무침전 순환방식에 의한 방류수의 부유물질 상승현상 등을 억제할 수 있는 효과도 갖게 된다.The present invention relates to a wastewater treatment apparatus by a catalytic oxidation method, and in the present invention, in the wastewater treatment apparatus by a catalytic oxidation method including a sedimentation tank, a screen tank, a decay tank, a flow rate adjustment tank, a contact aeration tank, a precipitation tank, and a sterilization discharge tank, The contact aeration tank is filled with chitosan-coated chitosan contact material and is divided into four or more tanks so that the organic cistern in the waste water can be adsorbed and decomposed by bacteria cilia in the first tank, photosynthetic bacteria in the second tank, and algae after the third tank. Provided is a wastewater treatment apparatus using a chitosan contact material, which is made. The contact aeration tank constructed in accordance with the present invention has an excellent wastewater treatment effect by facilitating the adhesion of biofilm and contaminants on the chitosan contact material, thereby facilitating the digestion and decomposition of the contaminants. There is also an effect that can suppress the rise phenomenon.

Description

키토산 접촉재를 이용한 오폐수 처리장치 {Waste Water Treatment System Using Chitosan Media}Wastewater Treatment System Using Chitosan Contact Material {Waste Water Treatment System Using Chitosan Media}

본 발명은 접촉산화법에 의한 오폐수 처리장치에 관한 것, 특히 접촉폭기조를 4실 이상으로 구분하여 구성하고 여기에 양이온적 성질을 지닌 키토산을 코팅한 접촉재를 충진시킨 오폐수 처리장치에 관한 것이다.The present invention relates to a wastewater treatment apparatus by a catalytic oxidation method, and more particularly, to a wastewater treatment apparatus configured by dividing a contact aeration tank into four or more chambers and filling a contact material coated with chitosan having a cationic property thereto.

일반적으로 오폐수의 처리시스템에는 생물처리법, 물리화학처리법이 있으며 특히 유기성 오염물질의 처리에 많이 이용되고 있는 것이 생물처리법이다. 이 방법은 자연의 자정작용을 응용해서 미생물의 분해능력과 대사반응을 효율적으로 이용하는 방법이다. 생물처리법으로는 활성오니법, 장기폭기방법, 접촉처리방법 등이 있는데, 활성오니법은 최초침전지. 폭기조, 최후 침전지 및 활성오니 반송의 4단계로 구성하여 박테리아를 생식시킨 활성오니를 배수에 첨가해서 배수속의 유기물을 먹게한 후, 그 활성오니를 중량침전시켜 상등수를 방류하는 정화방법이다. 그러나 이 방법은 폭기조작이 운전관리의 대부분으로 작용하므로 조작의 안전성, 처리효율, 유지관리의 난이성 등의 불편과 전문기술자가 항시 근무하여야 하고 넓은 공간을 필요로 한다는 단점이 있다. 장기폭기방법은 활성오니법의 편법으로 표준적인 방법보다도 폭기시간이 길고 BOD부하가 작고, 폭기 혼합액의 부유물 농도가 높게 유지되는 것이 특징이지만 활성오니법과 마찬가지로 오니의 반송을 수행한다는 점에서 크게 향상된 점이 없는 방법이다.In general, there are biotreatment methods and physicochemical treatment methods for wastewater treatment systems. In particular, biotreatment methods are widely used for treating organic pollutants. This method is a method of efficiently utilizing the microorganism's decomposition ability and metabolic reaction by applying the natural self-cleaning action. Examples of biological treatment methods include activated sludge method, long-term aeration method, and contact treatment method. It consists of four stages of aeration tank, final sedimentation basin, and returning of activated sludge, and adds activated sludge, which has lived with bacteria, to eat organic matter in the drainage, and then precipitates the activated sludge by weight precipitation to discharge the supernatant water. However, this method has the disadvantages that the aeration operation acts as a major part of operation management, and the inconvenience of operation safety, processing efficiency, and maintenance difficulty, and that a professional technician must work all the time and require a large space. The long-term aeration method is a short-acting method of activated sludge method, which is characterized by longer aeration time, less BOD load, and higher suspended solids concentration in the aeration mixture than the standard method. There is no way.

따라서, 이러한 문제를 해결하기 의한 방법으로 접촉처리방법이 개발되었는 바, 본 방법은 상기의 방법들과는 달리 폭기조로의 오니반송이 필요없는 방법이다. 이러한 접촉처리방법은 활성오니를 회전판 또는 고정사의 여러가지 매체에 미생물막으로 일정두께 부착시키고, 미생물막을 오수중의 유기물과 접촉시켜 흡착분해한다. 이때에 미생물의 호흡에 필요한 산소의 공급을 위해서 회전판의 경우에는 공기중에서 산소를 부착시키게 되고, 기타의 방법은 폭기에 의해 공급하는 바, 메디아에 부착된 미생물막이 두꺼워지면 회전판의 경우는 회전전단에 의하여, 기타의 경우는 폭기에 의하여 탈락되어 최종침전지에서 고액분리시켜 처리하는 공법이다.Therefore, the contact treatment method has been developed as a method to solve this problem, unlike the above method is a method that does not need to return the sludge to the aeration tank. Such a contact treatment method attaches activated sludge to a variety of media on a rotating plate or a fixed yarn with a microbial membrane, and adsorbs and decomposes the microbial membrane by contacting organic matter in sewage. At this time, in order to supply oxygen necessary for the respiration of microorganisms, the rotating plate attaches oxygen in the air, and other methods are supplied by aeration. When the microbial film attached to the media becomes thick, the rotating plate is attached to the rotating shear. In other cases, it is a method of dropping off by aeration and treating by solid-liquid separation from the final settler.

이러한 공법의 대표적인 방식으로는 회전원판 접촉법과 접촉산화법 등이 있다. 상기 처리공법들은 활성오니법의 장기폭기방법보다 상당히 진보된 공법이지만 설계와 시공기술상 다음과 같은 고도의 기술 습득이 요구되는 공법이다. 즉,Representative methods of such a method include a rotating disk contact method and a contact oxidation method. The treatment methods are considerably more advanced methods than the long-term aeration method of the activated sludge method, but they require a high level of skill in design and construction techniques. In other words,

(1) 전달력에 의한 미생물의 부착 불량방지(1) Prevention of adhesion of microorganisms by transmission force

(R.B.C(회전원판접촉기): 회전전달력, 기타방법: 폭기에 의한 수격 전단력)(R.B.C (rotary disc contactor): rotation transfer force, other method: water hammer shear force by aeration)

(2) 메디아의 재질선택(2) Material selection of media

(3) R.B.C법의 경우 원판의 최종 회전단력에 의한 회전축과 기계부하 등이다. 특히, 메디아의 재질 성분은 활성오니 처리의 최대요건인 지표미생물의 생성에 좌우되므로 왼전무독한 재질성분을 선택하여야 하며, 이 경우 최대의 해결문제는 재질의 강도, 영구성 및 부착능력 등에 달려 있다.(3) In the case of the R.B.C method, the rotation axis and mechanical load due to the final rotational end force of the disc. In particular, since the material composition of the media depends on the generation of surface microorganisms, which is the maximum requirement of activated sludge treatment, the leftmost nontoxic material components should be selected. In this case, the maximum resolution problem depends on the strength, permanence, and adhesion of the material.

따라서, 상기 공법이 진보된 공법이면서도 전반적으로 활용되지 못하는 이유는 메디아의 재질 및 활성오니의 부착능력과 탈리현상의 문제를 해결하지 못하고있기 때문이다.Therefore, the reason why the above method is not an advanced method but is generally used is because it does not solve the problem of adhesion and detachment of media and active sludge.

한편, 일반적으로 보급되어 있는 접촉산화법을 이용하는 시스템에 설치된 침전조는 활성오니법이나 장기폭기방법에서 볼 수 있는 오니의 반송을 필요로 하지 않으면서 접촉폭기조에서의 유출수의 미량부유물 제거와 미생물막의 잉여 축적에 의한 유출 혹은 여상세정에 의한 오니유출 등에 의한 처리수질 악화를 방지하기 위하여 설치된다. 그러나, 종래 처리수의 상부 유입을 통하여 침전조에 가해지는 수면적 부하에 의하여 부유물질의 상승이 발생하여 방류수 수질의 악화가 초래되고, 이를 방지하기 위하여 침전조 용량의 확대로 인한 부지 및 비용의 증가를 발생시키고 있는 문제를 지니고 있다.On the other hand, the sedimentation tank installed in the system using the commonly used catalytic oxidation method removes traces of effluent and the accumulation of excess microbial membrane in the contact aeration tank without requiring the return of sludge as seen in the activated sludge method or the long-term aeration method. It is installed in order to prevent the deterioration of treated water quality due to the outflow by or the sludge outflow due to filter cleaning. However, due to the surface load applied to the sedimentation tank through the upper inflow of the treated water, rise of suspended solids causes deterioration of the quality of the discharged water, and in order to prevent the increase of the site and cost due to the expansion of the sedimentation tank capacity. I have a problem that's happening.

따라서, 상기의 문제를 해결하기 위하여 본 발명에서는 접촉산화시스템에 있어서 접촉폭기조의 접촉재 상에 생물막 및 오염물의 부착이 원활히 이루어지고 이로 인한 오염물의 소화분해가 촉진될 수 있도록, 접촉폭기조를 4실 이상으로 구분하여 구성하고 여기에 기존의 표면적에 의한 접촉방식과 아울러 전하에 의한 접촉방식이 함께 작용할 수 있도록 양이온적 성질을 갖는 키토산을 코팅시킨 오폐수 처리장치를 제공하는데 그 목적이 있다.Therefore, in order to solve the above problems, in the present invention, four contact aeration tanks are provided so that the biofilm and contaminants can be smoothly adhered to the contact material of the contact aeration tank in the contact oxidation system, thereby facilitating the digestion and decomposition of the contaminants. It is an object of the present invention to provide a wastewater treatment apparatus coated with chitosan having a cationic property so that the above-described structure and the contact method by the surface area as well as the contact method by the charge can work together.

또한 본 발명은 접촉산화시스템에 있어서 통상 접촉폭기조 후단에 설치되는 침전조를 무침전 순환방식으로 대치하여 접촉폭기조를 통과한 처리수를 하부로 유입시킴과 동시에 이 유입수를 스프레이 분무방식으로 다시 접촉폭기조로 순환시킴으로써 수면적부하에 의한 부유물질의 상승을 억제할 수 있도록 하는 무침전 순환방식의 오폐수 처리장치를 제공하는데 그 목적이 있다.In the present invention, in the contact oxidation system, the sedimentation tank installed at the rear end of the contact aeration tank is replaced by the non-precipitating circulation method to introduce the treated water that has passed through the contact aeration tank to the bottom, and at the same time, the inflow water is sprayed back into the contact aeration tank. It is an object of the present invention to provide a wastewater treatment apparatus of a non-precipitating circulation system that can suppress a rise of suspended solids due to surface area load by circulating.

도 1은 본 발명의 무침전 순환방식의 오폐수 처리공정을 나타낸 흐름도이고,1 is a flow chart showing a wastewater treatment process of the non-precipitating circulation method of the present invention,

도 2는 본 발명의 무침전 순환방식의 오폐수 처리시스템의 모식도를 나타낸 것이고,Figure 2 shows a schematic diagram of the wastewater treatment system of the non-precipitating circulation method of the present invention,

도 3은 본 발명의 오폐수 처리공정에 이용되는 순환조 원리를 나타낸 것이다.Figure 3 shows the principle of the circulation tank used in the wastewater treatment process of the present invention.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

10: 침사조 20: 스크린조10: tide tank 20: screen tank

30: 부패조 40: 유량조정조30: corruption tank 40: flow adjustment tank

50: 접촉폭기조 60-1: 처리수 순환라인50: contact aeration tank 60-1: treatment water circulation line

60: 순환조 70: 소독방류조60: circulation tank 70: disinfection discharge tank

상기의 목적을 달성하기 위하여 본 발명에서는,침사조, 스크린조, 부패조, 유량조정조, 접촉폭기조, 침전조 및 살균방류조를 포함하는 접촉산화법에 의한 오폐수 처리장치에 있어서,상기 접촉폭기조는 키토산이 코팅된 키토산접촉재로 충진되고 4조 이상으로 구분되어 1차조에서는 박테리아섬모, 2차조에서는 광합성 세균, 3차조 이후에서는 조류에 의해 오폐수에 포함된 유기물이 흡착분해될 수 있도록 이루어진 것을 특징으로 하는 키토산 접촉재를 이용한 오폐수 처리장치가 제공된다.본 발명의 일 실시예에서, 상기 침전조는 접촉폭기조를 통과한 처리수를 하부로 유입시키고, 하부로 유입된 처리수의 흐름을 이용한 와류현상으로 처리수에 포함된 오니 및 부유물질을 침전없이 다시 접촉폭기조로 순환시키는 무침전 순환방식으로 운영된다.본 명세서에서는 본 발명에 따라 무침전 순환방식으로 운영되는 침전조를 일명 "순환조"로 칭한다.In order to achieve the above object, in the present invention, in the wastewater treatment apparatus by the contact oxidation method, including a sedimentation tank, screen tank, decay tank, flow adjustment tank, contact aeration tank, sedimentation tank and sterilization discharge tank, the contact aeration tank is chitosan It is filled with coated chitosan contact material and divided into 4 trillion or more, and chitosan, characterized in that it is made to adsorb and decompose organic matter contained in wastewater by bacterial cilia in the first tank, photosynthetic bacteria in the second tank, and algae after the third tank. Provided is a wastewater treatment apparatus using a contact material. In one embodiment of the present invention, the settling tank introduces the treated water that has passed through the contact aeration tank to the lower side and the treated water as a vortex phenomenon using the flow of the treated water introduced to the lower side. It operates in a non-precipitating circulation system in which sludge and suspended solids contained in the product are circulated back to the contact aeration tank without sedimentation. In the present invention, the sedimentation tank operated in the non-precipitating circulation method according to the present invention is referred to as "circulation tank".

이하, 본 발명의 키토산 접촉재에 대하여 구체적으로 설명하면 다음과 같다.Hereinafter, the chitosan contact member of the present invention will be described in detail.

오폐수 처리에 사용되는 접촉재를 적절히 선택하여 사용하는 것은 접촉폭기법의 성패를 좌우하는 가장 중요한 요소이다.Proper selection and use of contact materials used in wastewater treatment is the most important factor in determining the success or failure of the contact aeration method.

최근에는 접촉산화방법의 접촉재를 바이오레타, 바이오큐 또는 현수미생물 접촉방법 등의 각종 접촉재를 충진사용하고 있으나, 폭기전단력에 의한 미생물막의 부착성, 재질의 엉킴패쇄 파손과 산기관의 교체방안 등 여러가지 기술적인 면이 검토되어야 하는 것으로 평가되고 있으며 유기물의 부하량 조사설정에 있어서 생활오수의 경우에는 BOD량은 물론이고 SS(고형물질)량도 유기물 부하량으로 포함시켜야 하고, 부착능력을 특히 고려하여야 한다.Recently, various types of contact materials, such as bioreta, biocue, or suspension microorganism contact method, have been used for the contact oxidation method, but the adhesion of microbial membranes due to aeration shear force, breakage of tangles of materials, and replacement of diffusers It is evaluated that various technical aspects should be reviewed, and in the case of setting up a survey of loads of organic matter, the amount of solid matter (SS) as well as BOD should be included as organic load in the case of living sewage. do.

이에 본 발명자는 접촉폭기조에서의 폭기전단력에 의한 미생물막의 부착성 및 오니의 탈리현상을 방지할 수 있는 방법을 연구한 결과, 자연계에서 존재하면서 인체에 무해하고 양이온적(+) 성질을 갖는 키토산을 주목하게 되었다.Therefore, the present inventors studied a method for preventing the adhesion of microbial membranes and sludge detachment due to the aeration shear force in the contact aeration tank. As a result, the present inventors found that chitosan, which is present in nature and harmless to the human body, has a cationic (+) property. It became noticeable.

키토산은 천연물 가운데 유일하게 아미노기(NH2+)를 가진 (+)이온의 성질을가진다. 이러한 양이온적 성질의 아민그룹은 (-)이온과 반응하기 쉽다. 흥미롭게도 세균이나 바이러스는 (-)이온인 카르복실기(COO-)기를 가지고 있어 고분자 키토산의 (+)이온과 만나면 쉽게 결합하게 된다.Chitosan is the only natural product that has the property of (+) ion with amino group (NH 2+ ). Amine groups of this cationic nature are likely to react with negative (-) ions. Interestingly, bacteria or viruses (-) ion, a carboxyl group (COO -) groups will easily got coupled meet with (+) ions in the chitosan polymer.

따라서 상기 키토산을 접촉재에 코팅하여 사용하면, 접촉재에 부착된 미생물 막균이 접촉재의 재질과 성질로 인하여 탈락하지 않고 미생물균, 즉 부착된 오니의 내부층에서 잉여오니를 소화분해시키므로써 잉여오니를 발생하지 않게 된다. 특히 본 발명의 키토산 접촉재가 수중에서 윤상의 방사성으로 형성되면서 대전하를 띄게되고 오수중의 유기물을 적극 흡착함으로써 오니와 유기물의 부착이 잘되어 유기물의 처리효율이 높고 저농도에서 고농도의 오수까지도 처리가 가능하게 된다. 아울러 키토산 접촉재는 기존의 표면적에 의한 접촉방식에 더하여 전하에 의한 접촉방식이 함께 작용하게 되므로 미생물의 부착능력 및 탈리방지를 크게 개선 할 수 있게 된다.Therefore, when the chitosan is coated on the contact material, the microbial membranes adhered to the contact material do not fall off due to the material and properties of the contact material, and the surplus sludge is digested by digesting the surplus sludge in the inner layer of the attached sludge. Will not occur. In particular, the chitosan contact material of the present invention is formed in the form of a radioactive radioactively in water, exhibits a charge charge and actively adsorbs organic matter in sewage, so that adhesion of sludge and organic matter is good, so that the treatment efficiency of organic matter is high, and even low to high concentration sewage can be treated. Done. In addition, the chitosan contact material, in addition to the conventional contact method by the surface area, the contact method by the charge acts together can greatly improve the adhesion ability and desorption prevention of the microorganism.

이하 본 발명의 키토산 접촉재를 사용한 무침전 순환방식의 오폐수처리공정을 일 실시예를 들어 구체적으로 설명하면 다음과 같다.(도 1 및 도 2)Hereinafter, the wastewater treatment process of the non-precipitating circulation method using the chitosan contact material of the present invention will be described in detail with reference to one embodiment. (FIGS. 1 and 2)

본 실시예의 오폐수 처리공정에서는 계획오수량을 100m3/일로 설정하였으며, BOD 유입량 200ppm, SS(부유물질)유입량 200ppm으로 하여 BOD 및 SS의 방류수 수질이 모두 20ppm 이하가 되게 하여 제거율이 90% 이상이 되도록 설계하였다.In the wastewater treatment process of this embodiment, the planned wastewater amount was set to 100m 3 / day, and the BOD inflow rate was 200ppm and SS (floating material) inflow rate was 200ppm, so that both the discharged water quality of BOD and SS was 20ppm or less so that the removal rate was 90% or more. Designed.

침사조(10)Tide Tide (10)

유입 오수중에 함유된 비중이 큰 협잡물을 제거한다. 즉, 수중의 모래, 자갈 및 금속물질 등을 제거하여 펌프 등 기계장치나 관의 마모 및 폐쇄를 막고 침전조나 슬러지 소화조내에 축적되어 처리효율을 저하시키는 것을 방지한다.Eliminates heavy contaminants in influent sewage. In other words, it removes sand, gravel, and metals from the water to prevent abrasion and closure of machinery and pipes such as pumps, and to accumulate in sedimentation tanks or sludge digesters to prevent degradation of treatment efficiency.

스크린조(20)Screen Joe (20)

수처리의 첫단계로서 오수처리장으로 유입되는 오수중에 포함되어 있는 각종 부유물질중 조대물을 제거하여 펌프나 기계설비의 손상을 방지하기 위해 설치한다.As the first step of water treatment, it is installed to prevent the damage of pump or mechanical equipment by removing coarse substances from various suspended substances contained in sewage flowing into sewage treatment plant.

부패조(30)Corruption (30)

침전 및 소화가 한 탱크내에서 동시에 진행되나 침전실과 소화실이 분리되어 있지 않고, 과대한 부하나 간헐적인 부하를 받아들이는 능력이 우수하도록 제작하였다.Sedimentation and extinguishing proceed simultaneously in a tank, but the sedimentation and extinguishing chambers are not separated, and are designed to be capable of accepting excessive or intermittent loads.

유량조정조(40)Flow Adjustment Tank (40)

유입되는 오수를 일단 저류시키고 협잡물 및 스컴의 유입을 방지하고, 시간의 변화에 따른 수의 유량 및 농도의 변화를 최소화하는 것이 주기능이다. 공정중 일부 다른기능으로서 추가 설비된다. 시간당 오수량은 평균오수량의 1.5/24배, 오수배출 시간을 12시간으로 가정하여 필요용량을 24.6m3가 되도록 하였다.The main function is to store the incoming sewage once, prevent the inflow of contaminants and scum, and minimize the change of the flow rate and concentration of the water with the change of time. Some other functions are added during the process. The amount of sewage per hour was 1.5 / 24 times the average amount of sewage and the discharge time was assumed to be 12 hours so that the required capacity was 24.6m 3 .

접촉폭기조(50)Contact Aeration Tank (50)

활성슬러지에 의한 유기성물질의 산화, 슬러지의 증식, 자기산화 등 생물학적인 반응을 진행시키고 유기물을 제거하기 위해 이에 필요한 공기(산소)를 주입하고 교반하는 시설이다. 또한 본 발명의 키토산 접촉재가 각각의 실에 충진되어 사용되는 곳으로서, 4실로 구분된 각각의 조에서 오수 중에 포함된 유기성 물질, 중금속을 처리하게 된다. 즉 1차조에는 박테리아섬모, 2차조에는 광합성 세균, 3차조 이후는 조류에 의해 유기물을 흡착분해시켜 처리효율을 높이고, 난해성 BOD 물질인 질소 및 인까지도 제거할 수 있게 된다. 이와같은 오염물질의 제거효율은 이후 설명하게 될 순환조의 처리수 순환라인(60-1)의 처리수 재순환을 통하여 키토산 접촉재와의 접촉률이 더욱 증가하게 되어 키토산 접촉재 자체의 재질 및 성질과 더불어 오염물질의 제거 기능을 배가할 수 있다.It is a facility that injects and stirs the air (oxygen) necessary for the progress of biological reactions such as oxidation of organic substances by activated sludge, growth of sludge, and self-oxidation and removal of organic substances. In addition, as the chitosan contact material of the present invention is used to fill each chamber, it is to treat the organic material, heavy metals contained in the sewage in each tank divided into four chambers. That is, in the first tank, bacteria cilia, in the second tank, photosynthetic bacteria, and after the third tank, the organic matter is adsorbed and decomposed by algae to increase the treatment efficiency, and to remove nitrogen and phosphorus, which are difficult-to-dissolve BOD substances. The removal efficiency of such contaminants is further increased through the treatment water recycling of the treatment tank circulation line 60-1 of the circulation tank, which will be described later, so that the contact rate with the chitosan contacts is further increased. It can double the function of removing pollutants.

접촉폭기조의 유효용량 및 접촉재의 길이는 다음 표 1에 의거 선정한다.The effective capacity of the contact aeration tank and the length of the contact material are selected according to the following table 1.

시 설 규 모(M3/일)Facility size (M 3 / day) 용적부하(BOD 및 SS의 합)(KG/M3)Volume load (sum of BOD and SS) (KG / M 3 ) 현수미생물 접촉재의 부하(제거BOD 및 SS의 합)(8/M일)Load of suspension microbial contact (sum of removed BOD and SS) (8 / M days) 100미만Less than 100 0.5 - 0.80.5-0.8 5 - 85-8 100이상-500미만100 to over 500 0.8 - 1.20.8-1.2 8 - 128-12 500이상-1000미만500 or more-less than 1000 1.2 - 1.51.2-1.5 12 - 1612-16 1000이상More than 1000 1.5 - 2.01.5-2.0 16 - 2516-25

각 조의 유효용량(4실 이상으로 구분)Effective capacity of each group (we divide into four rooms or more)

제1조: 40% 제2조: 30% 제3,4조: 15%Article 1: 40% Article 2: 30% Article 3, 4: 15%

접촉재의 충진율: 55% 이상Filling rate of contact material: more than 55%

조내 용존산소 유지농도: 1 PPM 이상Dissolved oxygen maintenance concentration in the tank: 1 PPM or more

유효수심: 1.5∼5M 이하Effective depth: 1.5 ~ 5M or less

필요용량(BOD + SS의 용적부하로 계산)Required capacity (calculated as volume load of BOD + SS)

따라서, 접촉폭기조의 각 실별 유효용량을 계산하면Therefore, if you calculate the effective capacity of each room in the contact aeration tank

제1실 32M3, 제2실 24M3, 제3실 12M3, 제4실 12M3 Room 1 32M 3 , Room 2 24M 3 , Room 3 12M 3 , Room 4 12M 3

접촉재의 길이(제거 BOD = 180PPM, 제거 SS = 180PPM)임을 감안하여Given that the length of the contact material (removed BOD = 180PPM, removed SS = 180PPM)

이며, 각 실별 접촉재의 길이는The length of the contact material for each thread is

제1실: 1.800M, 제2실 1.350M, 제3실 0.675M, 제4실 0.675M이 된다.1st room: 1.800M, 2nd room 1.350M, 3rd room 0.675M, 4th room 0.675M.

순환조(60)Circulation tank (60)

종래 침전조의 수면적 부하 때문에 발생하는 SS(부유물질) 및 슬러지 부상을 방지할 수 있으며 통상 중상부의 내통으로 유입되는 관념에서 벗어나 도 3에 나타낸 바와 같이 하부에서 처리수를 유입하는 방식을 채택하였으며 순환조로 일부의 오니가 유입되었다 하더라도 순환조의 구조적 특징에 의하여 접촉폭기조로 다시 오니가 흘러 들게 되어있다. 즉, 폭기조에서의 물의 흐름을 이용한 와류현상으로 슬러지 및 부유물질을 가장 안정적으로 관리할 수 있는 기능을 가지며 기존 침전조의감속기, 슬러지 수집기 및 내통이 필요없는 탱크이다.It can prevent SS (floating material) and sludge injuries caused by the surface load of the conventional sedimentation tank, and in general, the process water is introduced from the bottom as shown in FIG. Even if some sludge flows into the tank, sludge flows back into the contact aeration tank due to the structural characteristics of the circulation tank. That is, it is a tank that has the function to manage the sludge and the suspended solids most stably by the vortex phenomenon using the flow of water in the aeration tank, and does not need the reducer, the sludge collector and the inner cylinder of the existing sedimentation tank.

소독방류조(70)Disinfection Disposal Tank (70)

살균 작용 및 처리수를 배출하는 기능을 가진다.It has a function of disinfecting and discharging treated water.

상술한 바와 같이 본 발명의 키토산 접촉재는 표면적 향상 위주의 기존 접촉재에 양이온적 성질을 갖는 키토산을 코팅하여 사용함으로써 접촉재에 정전기적 힘이 함께 작용하도록 하고, 순환조의 설치에 의하여 처리수의 이동경로를 효율적으로 운영함으로써 다음과 같은 효과를 얻게 된다.As described above, the chitosan contact material of the present invention is coated with chitosan having a cationic property on the existing contact material mainly for surface area improvement, so that the electrostatic force acts on the contact material, and the treatment water is moved by installing a circulation tank. By operating the route efficiently, you will:

① 키토산 접촉재에 오니부착을 극대화 할 수 있다.① Maximize sludge adhesion to chitosan contact material.

② 방류수의 부유물질 상승현상을 억제할 수 있다.② It can suppress the rise of suspended solids in effluent.

③ 침전조의 용량부족 해소를 위한 침강성 향상을 기할수 있다.③ It is possible to improve the sedimentation to solve the capacity shortage of the settling tank.

④ 방류되는 중금속을 월등하게 흡착하여 안정적 수질확보가 가능하다.④ It is possible to secure stable water quality by absorbing heavy metals discharged.

⑤ pH가 약산성으로 유지되어 pH부하를 최소화할 수 있다.⑤ The pH is kept slightly acidic to minimize the pH load.

⑥ 벌킹 및 자산화에 의한 SV상승 및 슬러지의 월류현상을 개선할 수 있다.⑥ It can improve SV rise and sludge overflow caused by bulking and assetization.

Claims (3)

삭제delete 침사조, 스크린조, 부패조, 유량조정조, 접촉폭기조, 침전조 및 살균방류조를 포함하는 접촉산화법에 의한 오폐수 처리장치에 있어서,In the wastewater treatment apparatus by the catalytic oxidation method including a sedimentation tank, a screen tank, a decay tank, a flow regulating tank, a contact aeration tank, a precipitation tank and a sterilization discharge tank, 상기 접촉폭기조는 키토산이 코팅된 키토산접촉재로 충진되고 4조 이상으로 구분되어 1차조에서는 박테리아섬모, 2차조에서는 광합성 세균, 3차조 이후에서는 조류에 의해 오폐수에 포함된 유기물이 흡착분해될 수 있도록 이루어진 것을 특징으로 하는 키토산 접촉재를 이용한 오폐수 처리장치.The contact aeration tank is filled with chitosan-coated chitosan contact material and is divided into four or more tanks so that the organic cistern in the waste water can be adsorbed and decomposed by bacteria cilia in the first tank, photosynthetic bacteria in the second tank, and algae after the third tank. Wastewater treatment apparatus using a chitosan contact material, characterized in that made. 제2항에 있어서,The method of claim 2, 상기 침전조는 접촉폭기조를 통과한 처리수를 하부로 유입시키고, 하부로 유입된 처리수의 흐름을 이용한 와류현상으로 처리수에 포함된 오니 및 부유물질을 침전없이 다시 접촉폭기조로 순환시켜 무침전 순환방식으로 운영되는 것을 특징으로 하는 오폐수 처리장치.The sedimentation tank is introduced into the lower portion of the treated water passed through the contact aeration tank, and the sludge and suspended solids contained in the treated water are circulated to the contact aeration tank without sedimentation as a vortex phenomenon using the flow of the treated water introduced into the lower portion. Waste water treatment apparatus, characterized in that operated in a manner.
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