KR101278101B1 - Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same - Google Patents

Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same Download PDF

Info

Publication number
KR101278101B1
KR101278101B1 KR1020110013275A KR20110013275A KR101278101B1 KR 101278101 B1 KR101278101 B1 KR 101278101B1 KR 1020110013275 A KR1020110013275 A KR 1020110013275A KR 20110013275 A KR20110013275 A KR 20110013275A KR 101278101 B1 KR101278101 B1 KR 101278101B1
Authority
KR
South Korea
Prior art keywords
activated carbon
fiber material
adhesive resin
decomposition
carbon contact
Prior art date
Application number
KR1020110013275A
Other languages
Korean (ko)
Other versions
KR20120093610A (en
Inventor
이종열
최삼룡
Original Assignee
아름다운 환경건설(주)
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 아름다운 환경건설(주) filed Critical 아름다운 환경건설(주)
Priority to KR1020110013275A priority Critical patent/KR101278101B1/en
Publication of KR20120093610A publication Critical patent/KR20120093610A/en
Application granted granted Critical
Publication of KR101278101B1 publication Critical patent/KR101278101B1/en

Links

Images

Classifications

    • 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
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F3/103Textile-type packing
    • 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
    • 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

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Water Treatment By Sorption (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

본 발명은 유기물 흡착분해용 활성탄접촉여재에 관한 것으로, 보다 상세하게는, 성형된 활성탄 입자와 용융이 쉬운 폴리에테르나 폴리에스테르 등의 단섬유를 혼합하여 용융성형하거나, 아크릴이나 에폭시 접착수지를 혼합하여 성형된 유기물 흡착분해용 활성탄접촉여재 및 이를 이용한 비점오염물질 정화용 수처리장치에 관한 것이다.  The present invention relates to activated carbon contact media for adsorptive decomposition of organic matter, and more particularly, melt-molded by mixing shaped activated carbon particles and short fibers such as polyether or polyester that are easy to melt, or mixing acrylic or epoxy adhesive resins. The present invention relates to an activated carbon contact medium for adsorptive decomposition of molded organic materials and a water treatment apparatus for purifying nonpoint pollutants using the same.

Description

유기물 흡착분해용 활성탄접촉여재 및 이를 이용한 비점오염물질 정화용 수처리장치{Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same}  Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same}

본 발명은 유기물 흡착분해용 활성탄접촉여재에 관한 것으로, 보다 상세하게는, 활성탄 입자, 용융이 쉬운 폴리에테르나 폴리에스테르 등의 섬유재를 혼합 성형하거나, 아크릴이나 에폭시 접착수지를 혼합하여 성형된 유기물 흡착분해용 활성탄접촉여재 및 이를 이용한 비점오염물질 정화용 수처리장치에 관한 것이다.   The present invention relates to an activated carbon contact medium for adsorptive decomposition of organic matter, and more particularly, an organic material formed by mixing and molding activated carbon particles and fiber materials such as polyether or polyester that are easy to melt, or by mixing acrylic or epoxy adhesive resins. The present invention relates to an activated carbon contact filter for adsorption decomposition and a water treatment apparatus for non-point pollutant purification using the same.

일반적으로, 오염물질은 생활하수, 산업폐수 및 축산폐수 등과 같이 배출지점이 뚜렷하고 한정된 점오염원(點汚染源)으로부터 배출되는 점오염물질과 불특정지역의 농경지, 목초지, 산림지, 건축현장, 광산, 벌채지, 폐기물처리장, 쓰레기매립장, 도심지, 도로, 및 산업현장 등과 같이 배출지역이 불특정적이고 광범위한 비점오염원(非點汚染源)으로부터 배출되는 비점오염물질로 나눌 수 있다.  Generally, pollutants include point pollutants emitted from well-defined and limited point sources, such as domestic sewage, industrial waste and livestock waste, and agricultural land in unspecified areas, grasslands, forests, construction sites, mines, logging sites, Discharge areas can be divided into nonpoint pollutants emitted from an unspecified and widespread nonpoint source, such as waste disposal sites, landfills, urban areas, roads, and industrial sites.

이 중, 종래의 비점오염물질 처리기술로는 수평으로 격벽을 설치하여 협잡물을 제거하기 위한 세목스크린을 설치하고 각종 안트라싸이트 또는 활성탄과 같은 여재를 통과시켜 오염원을 제거하는 기술이 있으며, 기타 종래 기술로는 모래, 활성탄, 안트라싸이트와 같은 여재층을 형성시켜 우수가 위에서 아래 방향으로 여재를 거쳐 유출되도록 하거나 하부에서 상부로 여재층을 통과시켜 유출되도록 하는 기술이 있다. Among them, the conventional non-point pollutant treatment technology includes a screen for removing contaminants by installing a partition horizontally and removing contaminants by passing through various media such as anthracite or activated carbon, and other conventional technologies. Furnace has a technology that forms a layer of media such as sand, activated carbon, anthracite so that rainwater flows through the media from top to bottom or through the media from bottom to top.

그러나, 이들 종래 기술은 여재의 비중이 물보다 크며, 여재가 고정식으로 충전되어 있어 우수 유입시 미세탁도에 의해서 여재층이 막히는 현상이 나타날 뿐만 아니라 여재를 교환이나 역세척하는 데 많은 어려움이 있다.  However, these prior arts have a specific gravity of the filter medium larger than water, and the filter medium is filled in a fixed manner so that the filter layer is clogged due to fine turbidity at the time of rain.

현재, 우수처리장치에 사용되는 오염물질 처리용 접촉여재는 표면적이 상대적으로 넓고 만들기 쉬운 활성탄 부직포, 내구성이 높고 공극을 만들기 쉬운 황토나 세라믹, 나무를 이용한 우드칩, 성형이 자유롭고 비중이 가벼운 플라스틱을 이용한 접촉여재가 다양하게 개발되어 있으며, 아울러, 이러한 접촉여재가 적용된 수처리장치도 다양하게 개발되고 있다. 그러나, 이들의 공통점은 미생물부착이 가능한 공극을 최대한으로 증대시켜 미생물의 성장을 안정화시키고 빈부하나 과부하 등의 충격부하에 견딜 수 있도록 구성하였으나, 쉽게 신축되거나, 탈리현상이 나타나거나, 부착이 쉽지 않거나, 2차오염을 일으키거나, 제조비용이 고가인 문제점 등이 있다.  Currently, the contact media for treating pollutants used in rainwater treatment devices are made of activated carbon nonwoven fabric having a relatively large surface area and easy to make, loess, ceramic, wood chips made of wood, which are easy to make pores, and plastic freely formed and light in specific gravity. Various contact media have been developed, and a variety of water treatment apparatuses to which such contact media have been applied have also been developed. However, their commonality is to increase the voids that can be attached to the microorganisms to the maximum, to stabilize the growth of the microorganisms and to withstand impact loads such as poor loads or overloads, but they are easily stretched, desorption, or difficult to attach. There is a problem that causes secondary pollution, or expensive manufacturing costs.

따라서, 이러한 문제점에 착안하여 지금까지는 성형을 수 ㎛정도로 흡착하여 고착시킬 수밖에 없었던 접촉여재용 부직포를 대신하여 공극과 비표면적이 매우 크고 미생물의 성장에 장애를 주지 않으면서 쉽게 구할 수 있는 활성탄을 이용하여 용융이 쉬운 폴리에테르(PE)나 폴리에스테르(PET)의 폐섬유재와 혼합하여 용융성형하거나, 아크릴이나 에폭시 접착수지를 혼합하여 활성탄입자들을 일정 모양의 틀에 혼합해 넣고 상온 또는 가열 성형하여 다양한 모양으로 가공한 유기물 흡착분해용 활성탄접촉여재를 마련하여 수처리장치를 사용하면, 처리효율이 높은 처리수를 얻을 수 있을 뿐만 아니라 용존된 오염물도 쉽게 제거가능하여 고도처리가 되고 설비비와 운전비도 절감되어 경제적이면서도 처리효율이 극대화되어 환경오염을 저감시키게 되는 등의 효과가 얻어지는 수처리장치를 마련할 수 있다.  Therefore, in view of these problems, the use of activated carbon, which has a very large pore and specific surface area and does not interfere with the growth of microorganisms, is used instead of the nonwoven fabric for contact media, which has had to adsorb and fix the molding to a few μm so far. Melted by mixing with the waste fiber material of polyether (PE) or polyester (PET), which is easy to melt, or by mixing acrylic or epoxy adhesive resin and mixing activated carbon particles into a mold By using activated carbon contact media for adsorptive decomposition of organic materials processed into various shapes, using a water treatment device, not only can the treated water with high treatment efficiency be removed, but also the dissolved contaminants can be easily removed, resulting in high treatment and reduced equipment and operating costs. Economical and maximized treatment efficiency reduces environmental pollution The effect can be provided a water purifying apparatus is obtained.

따라서, 본 발명의 목적은 상기와 같은 종래의 문제점을 감안하여 안출한 것으로써, 활성탄 입자를 용융온도가 다른 폴리에테르나 폴리에스테르 등의 용융이 쉬운 섬유재와 혼합하여 용융하거나, 아크릴이나 에폭시 등의 접착수지를 혼합하여 일정형태로 가열성형한 다음 패키지화함으로써 미생물이 쉽게 접촉되어 생물막을 형성하여 유기물분해를 촉진하게 되며, 혐기 호기성 유기물 분해로 유기물은 물론 질소까지 제거시킴으로써 안정된 수처리가 가능하고, 아울러, 과부하나 빈부하 등의 충격부하에 대처하고 필요에 따라 모양과 공극을 자유로이 조절할 수 있도록 표면적을 극대화하고 부피를 조절함으로써 내구성을 확보하여 유지보수비용이 절감되고 경제적이면서도 처리효율이 극대화되는 유기물 흡착분해용 활성탄접촉여재 및 이를 이용한 비점오염물질 정화용 수처리장치를 제공하는 데 있다.  Accordingly, an object of the present invention is to devise in view of the above-described conventional problems, and the activated carbon particles are mixed and melted with easy-to-melt fiber materials such as polyether or polyester having different melting temperatures, or acrylic or epoxy or the like. By mixing the adhesive resin of the resin and heating it to a certain form and packaging it, microorganisms are easily contacted to form a biofilm to promote organic decomposition, and anaerobic aerobic decomposition of organic matter as well as nitrogen to remove the stable water treatment, In order to cope with the impact load such as overload or empty load, and to maximize the surface area and volume to adjust the shape and void freely as needed, it secures durability by reducing maintenance cost and maximizing economic efficiency and processing efficiency. Decomposition Activated Carbon Contact Media and Using the Same It is to provide a water treatment device for the purification of non-point pollutants.

상기와 같은 목적을 달성하기 위한 수단으로, 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재는 성형된 활성탄 입자와 폴리에테르 또는 폴리에스테르 등의 섬유재를 혼합하여 모형속에 놓고 섭씨 100~300도의 열로써 가열하여 저온용융 섬유가 용융되면서 활성탄입자를 접착시키거나 고온용융 섬유를 가교결합(crosslink)시켜 일정한 형태의 담체 또는 시트체로 형성된 것을 특징으로 한다.         As a means for achieving the above object, the activated carbon contact medium for adsorptive decomposition of organic matters according to the present invention is mixed with the molded activated carbon particles and a fiber material such as polyether or polyester and placed in a model as a heat of 100 ~ 300 degrees Celsius The low-temperature molten fiber is melted by heating to bond activated carbon particles or crosslink the high-temperature molten fiber to form a carrier or sheet body of a predetermined form.

또한, 본 발명의 다른 실시예에 따르면, 성형된 활성탄 입자와 폴리에테르 또는 폴리에스테르 등의 섬유재와 아크릴, 에폭시,초산비닐, PVC 등으로 된 접착수지를 이용할 수도 있다. In addition, according to another embodiment of the present invention, molded activated carbon particles, a fiber material such as polyether or polyester, and an adhesive resin made of acrylic, epoxy, vinyl acetate, PVC, or the like may be used.

나아가, 본 발명에 따른 비점오염물질 정화용 수처리장치는 집수조, 혐기조, 폭기조, 침전조, 여과조, 소독방류조를 포함하고, 상기 혐기조, 폭기조 및 여과조 내에 본 발명에 따른 상기한 유기물 흡착분해용 활성탄접촉여재를 장착시킨 것을 특징으로 한다.Furthermore, the apparatus for purifying non-point pollutants according to the present invention includes a collecting tank, an anaerobic tank, an aeration tank, a precipitation tank, a filtration tank, and a disinfection tank, and the activated carbon contact medium for adsorption decomposition of the organic matter according to the present invention in the anaerobic tank, aeration tank, and a filtration tank. It characterized in that the mounted.

이상에서 살펴본 바와 같이, 본 발명에 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재는, 표면적이 극대화되어 있는 활성탄을 자유자재로 성형하여 수처리에 적합하도록 담체화 또는 시트화하여 유지관리가 용이하며, 성형된 담체를 이용하여 미생물의 성장이 안정되고 생물막을 쉽게 형성하여 유기물분해를 원활히 수행할 수 있으며, 물리적 흡착여과기능을 수행하는 여과부를 갖춘 수처리장치에 상기한 활성탄접촉여재를 제공함으로써 폭기조 내에서 유기물 분해와 탈질이 동시에 이루어져 고도로 처리된 처리수를 얻을 수 있으며 동시에 시트를 통한 흡착여과까지 수행함으로써, 우수한 수처리와 함께 시설비와 운전비를 절감하여 경제적으로 환경오염을 저감시키는 효과가 있는 것이다.   As described above, the activated carbon contact medium for adsorptive decomposition of organic matters according to the present invention according to the present invention is easy to maintain and support by forming a activated carbon having a maximized surface area freely by carrier or sheeting to be suitable for water treatment, By using the molded carrier, the growth of microorganisms can be stabilized, biofilm can be easily formed, and organic decomposition can be performed smoothly, and the activated carbon contact filter is provided to the water treatment device equipped with a filtration unit that performs physical adsorption filtration function. Decomposition and denitrification at the same time to obtain a highly treated treated water and at the same time to perform the adsorption filtration through the sheet, it has the effect of reducing the environmental pollution economically by reducing the facility cost and operating costs with excellent water treatment.

도1은 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재의 모형도로서, (a)는 시트형 , (b)는 두루말이 담체형, (c)는 지구본 담체형의 모형도를 각각 예시하는 도면.
도2 및 도3은 본 발명의 다른 실시예에 따른 유기물 흡착분해용 활성탄접촉여재의 개략적인 측단면도.
도4는 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재를 이용하는 비점오염물질 정화용 수처리장치의 구성도.
1 is a schematic diagram of activated carbon contact media for organic material adsorption decomposition according to the present invention, (a) is a sheet type, (b) is a rolled carrier type, (c) is a diagram illustrating a model of a globe carrier type, respectively.
Figure 2 and Figure 3 is a schematic side cross-sectional view of the activated carbon contact medium for adsorption decomposition of organic matter according to another embodiment of the present invention.
4 is a block diagram of a water treatment apparatus for purifying non-point pollutants using activated carbon contact media for organic material adsorption decomposition according to the present invention.

이하, 본 발명의 바람직한 실시예를 첨부 도면을 참조하여 보다 상세하게 설명하면 다음과 같다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도1은 본 발명의 제 1 실시예에 따른 유기물 흡착분해용 활성탄접촉여재 담체(10)의 모형도를 다양하게 예시한다.  1 variously illustrates a schematic view of an activated carbon contact media carrier 10 for adsorption decomposition of organic matter according to a first embodiment of the present invention.

도1에서 보는 바와 같이, 본 발명의 제 1 실시예에 따른 유기물 흡착분해용 활성탄접촉여재(10)는 활성탄 입자(1)와 섬유재(2)로 구성된다. 구체적으로 설명한다면, 성형된 활성탄 입자(1)와 길이 5 ~ 10 ㎝의 폴리에테르 또는 폴리에스테르 섬유재 50 g/m2를 혼합하여 모형속에 넣고 섭씨 100~300℃의 열로써 가열하여 상기 폴리에테르 또는 폴리에스테르 섬유재(2)에 활성탄 입자(1)가 접착되어 일정한 형태, 예컨대, 도1(a)와 같은 시트형, 도1(b)와 같은 두루말이 담체형 및 도1(c)와 같은 지구본 담체형으로 형성되는 것이다. 특히, 도1(a)와 같은 시트형 활성탄접촉여재(10)는 상기 폴리에테르 또는 폴리에스테르 섬유재(2)를 직접 부직포로서 형성하거나 상기 섬유재보다 용융온도가 높은 별도의 부직포를 사용하여 그 내부에 활성탄 입자(1)를 충전시킨 것이다. 상기 시트형 활성탄접촉여재(10)는 롤(roll) 형태가 가능하여 폭과 깊이를 자유롭게 조절할 수 있고 담체의 교체도 쉽게 할 수 있다. As shown in FIG. 1, the activated carbon contact medium 10 for adsorptive decomposition of organic matter according to the first embodiment of the present invention is composed of activated carbon particles 1 and a fiber material 2. Specifically, the molded activated carbon particles (1) and 50 g / m 2 of polyether or polyester fiber material 5 to 10 cm in length are mixed in a model and heated with a heat of 100 ~ 300 ℃ Celsius to the polyether Alternatively, the activated carbon particles 1 are bonded to the polyester fiber material 2 to form a certain shape, for example, a sheet form as shown in FIG. 1 (a), a scroll type as shown in FIG. 1 (b), and a globe as shown in FIG. It is formed in a carrier form. In particular, the sheet-like activated carbon contact medium 10 as shown in FIG. 1 (a) may be formed by directly forming the polyether or polyester fiber material 2 as a nonwoven fabric or by using a separate nonwoven fabric having a higher melting temperature than the fiber material. It is filled with activated carbon particles (1). The sheet-like activated carbon contact medium 10 can be roll (roll) form can be freely adjusted the width and depth, and also easy to replace the carrier.

상기 유기물 흡착분해용 활성탄접촉여재(10)는 본 발명의 다른 실시예에 따라서 다양하게 제조될 수 있다.  The activated carbon contact medium 10 for adsorptive decomposition of organic matter may be variously manufactured according to another embodiment of the present invention.

본 발명의 제 2 실시예에 따른 유기물 흡착분해용 활성탄접촉여재는, 도 2에 도시된 바와 같이, 부직포 형태의 제1섬유재(2-1); 상기 제1섬유재(2-1) 상에 분사된 제1접착성 수지(3-1); 상기 제1접착성 수지(3-1) 상에 살포된 활성탄 입자(1); 상기 활성탄 입자(1) 위에 적층된 부직포 형태의 제2섬유재(2-2); 상기 제2섬유재(2-2) 상에 분사된 제2접착성 수지(3-2)를 포함하여 구성되며, 상기 제1섬유재(2-1)와 제1접착성 수지(3-1), 활성탄 입자(1), 제2섬유재(2-2) 및 제2접착성 수지(3-2)는 압력을 가하여 접착된다. 구체적으로, 부직포제조용 기계를 이용하여 폴리에스테르 섬유재(2)를 길이 5~10cm, 중량 50g/㎡ 으로 평평히 깔고 그 위에 아크릴 접착수지 용액(3)을 중량 10g/㎡으로 분사하고, 그 위에 입상활성탄 입자(1)를 높이 5±3mm, 중량 100g/㎡으로 뿌린 다음, 그 위에 다시 폴리에스테르 섬유재(2)를 길이 5~10cm, 중량 50g/㎡으로 깔고 아크릴수지(저온경화용)(3)를 중량 10g/㎡으로 분사한 후 일정압력으로 압착하여 상온에서 감아주면 시트가 완성된다. 필요에 따라 두께는 섬유, 활성탄 및 접착수지를 반복하여 적층시키면 두꺼워지며, 밀도를 높이려면 압착강도를 높이면 된다. 또한, 모양성형은 원하는 모양틀 속에 섬유와 활성탄과 수지를 혼합하여 상온에서 10분 내지 3시간 정도 굳히면 되고 굳히는 시간은 수지에 따라 다르다. 경우에 따라서는 빠른 성형가공을 위해 성형온도를 150℃ 범위까지 높일 수도 있다.Activated carbon contact media for organic adsorption decomposition according to a second embodiment of the present invention, as shown in Figure 2, the first textile material (2-1) of the nonwoven fabric form; A first adhesive resin 3-1 sprayed onto the first fiber material 2-1; Activated carbon particles 1 sprayed onto the first adhesive resin 3-1; A second fiber material 2-2 in the form of a nonwoven fabric laminated on the activated carbon particles 1; And a second adhesive resin 3-2 sprayed onto the second textile material 2-2, wherein the first textile material 2-1 and the first adhesive resin 3-1 are included. ), The activated carbon particles 1, the second fiber material 2-2 and the second adhesive resin 3-2 are bonded by applying pressure. Specifically, the polyester fiber material 2 was flattened with a length of 5 to 10 cm and a weight of 50 g / m 2 using a machine for producing a nonwoven fabric, and the acrylic adhesive resin solution 3 was sprayed thereon at a weight of 10 g / m 2, and thereon, Sprinkle the granular activated carbon particles (1) with a height of 5 ± 3mm and a weight of 100g / m2, and then lay the polyester fiber material (2) thereon with a length of 5 to 10cm and a weight of 50g / m2 and put an acrylic resin (for low temperature curing) ( 3) is sprayed at a weight of 10g / ㎡, compressed at a constant pressure and wound at room temperature to complete the sheet. If necessary, the thickness is increased by repeatedly stacking fibers, activated carbon and adhesive resin, and to increase the density, the compressive strength may be increased. In addition, the shape molding may be hardened at room temperature for 10 minutes to 3 hours by mixing fibers, activated carbon, and resin in a desired mold, and the time to harden varies depending on the resin. In some cases, the molding temperature may be increased to a range of 150 ° C. for rapid molding.

본 발명의 제 3 실시예에 따른 유기물 흡착분해용 활성탄접촉여재는, 도 3에 도시된 바와 같이, 본 발명의 제 2 실시예과 동일하게 구성하되, 상기 제1섬유재(2-1) 및 제2섬유재(2-2)는 고온 용해성 섬유재와 저온 용해성 섬유재가 혼합된 부직포로 형성되고, 상기 제1섬유재(2-1)와 제1접착성 수지(3-1), 활성탄 입자(1), 제2섬유재(2-2) 및 제2접착성 수지(3-2)는 열과 압력을 가해 접착된다. 구체적으로, 부직포제조용 기계를 이용하여 고온용해성 폴리에스테르 섬유재(2)를 길이 5~10cm, 중량 50g/㎡ 으로 그리고 저온용해성 폴리에테르(PE) 섬유재(2)를 중량 20g/㎡으로 혼합하여 평평히 깔고 그 위에 아크릴 접착수지 용액(3)을 중량 10g/㎡으로 분사하고, 그 위에 입상활성탄 입자(1)를 높이 5±3mm 및 중량 100g/㎡으로 뿌리고 그 위에 혼합섬유재(2)를 중량 70g/㎡으로 깔고 아크릴수지(저온경화용)(3)를 중량 10g/㎡으로 분사하여 챔버온도를 150℃±50로 유지하면서 일정압력으로 압착하여 상온에서 감아주면 시트가 완성된다. 시트의 두께는 상기 제2실시예에서와 마찬가지로 섬유, 활성탄 및 접착수지를 반복하거나 양을 증가시키면 두꺼워지고 밀도는 압착력에 의해 결정된다.Activated carbon contact medium for adsorption decomposition of organic matter according to the third embodiment of the present invention, as shown in Figure 3, is configured in the same manner as the second embodiment of the present invention, the first fiber material (2-1) and the first The second fiber material 2-2 is formed of a nonwoven fabric in which a high temperature soluble fiber material and a low temperature soluble fiber material are mixed, and the first fiber material 2-1, the first adhesive resin 3-1, and activated carbon particles ( 1), the second fiber material 2-2 and the second adhesive resin 3-2 are bonded by applying heat and pressure. Specifically, by using a nonwoven fabric manufacturing machine by mixing the high temperature soluble polyester fiber material (2) to 5 ~ 10cm in length, 50g / ㎡ in weight, and low temperature soluble polyether (PE) fiber material (2) to 20g / ㎡ by weight Lay flat and spray acrylic adhesive resin solution (3) on a weight of 10 g / m2, and spray the granular activated carbon particles (1) thereon at a height of 5 ± 3 mm and a weight of 100 g / m2, and mix the mixed fiber material (2) thereon. Spread it at 70g / m 2 and spray acrylic resin (for low temperature curing) 3 at a weight of 10g / m 2, compress the film at a constant pressure while maintaining the chamber temperature at 150 ° C. ± 50 to complete the sheet. As in the second embodiment, the thickness of the sheet is thickened by repeating or increasing the amount of fibers, activated carbon and adhesive resin, and the density is determined by the pressing force.

상기 실시예들에 있어, 활성탄 대신 중금속 흡착기능이 있는 기능성 섬유나 소독기능이 있는 섬유, 이온교환수지 등을 혼합하여도 기능성 부직포나 담체가 만들어진다.
In the above embodiments, a functional nonwoven fabric or carrier is made even by mixing functional fibers having a heavy metal adsorption function, disinfecting fibers, ion exchange resins, or the like instead of activated carbon.

상기와 같이 형성된 유기물 흡착분해용 활성탄접촉여재(10)를 담체 또는 시트형으로 구성함으로써, 활성탄 입자의 표면적을 섬유재를 이용하여 극대화시킬 수 있고, 아울러, 수처리에 적합하도록 자유자재로 성형하여 담체화 또는 시트화하여 유지관리가 용이하게 된다.       By forming the activated carbon contact medium 10 for adsorptive decomposition of organic matter formed as described above in a carrier or sheet form, the surface area of the activated carbon particles can be maximized using a fiber material, and formed into a free material so as to be suitable for water treatment. Alternatively, the sheet can be easily maintained.

도4는 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재를 이용하는 수처리장치의 구성도를 보여준다.       Figure 4 shows the configuration of the water treatment apparatus using the activated carbon contact medium for adsorption decomposition of organic matter according to the present invention.

도4에 도시된 바와 같이, 본 발명에 따른 유기물 흡착분해용 활성탄접촉여재를 이용한 비점오염물질 정화용 수처리장치(100)는, 크게는 집수조(101), 혐기조(102), 폭기조(103), 침전조(104), 여과조(105) 및 소독방류조(106)를 포함하고 있다.       As shown in FIG. 4, the apparatus for purifying non-point pollutants using activated carbon contact media for organic material adsorption decomposition according to the present invention includes a water collecting tank 101, an anaerobic tank 102, an aeration tank 103, and a precipitation tank. 104, a filtration tank 105 and a disinfection discharge tank 106 are included.

이들의 구성에 대해 구체적으로 설명하면, 일정한 형태의 집수조(101)에는 활성슬러지 등이 함유된 자연오염수가 유입되어 집수될 수 있도록 구비되고, 혐기조(102)에는 본 발명에 따른 담체형 활성탄접촉여재(10) 및 교반기(11)가 장착되고, 폭기조(103)에도 본 발명에 따른 활성탄접촉여재(10) 및 산기관(12)이 장착되고, 침전조(104)에서는 상기 폭기조(103)를 거친 물속에 함유된 슬러지를 침전시키고, 여과조(105)에는 내부에 본 발명에 따른 활성탄접촉여재(10)가 제공되며, 최종적으로 소독방류조(106)가 제공된다. 상기 혐기조(102) 및 폭기조(103) 내에 장착되는 활성탄접촉여재(10)는 담체형이 바람직하고, 상기 여과조(105) 내에 장착되는 활성탄접촉여재(10)는 시트형이 바람직하다. 상기 침전조(104)와 여과조(105) 사이에는 슬러지 펌프(13)가 제공되어 상기 침전조(104) 아래 가라 앉은 슬러지를 상기 혐기조(102)로 다시 보내 수처리과정을 반복하도록 하며, 슬러지를 거의 포함하지 않는 처리수는 여과조(105) 및 소독방류조(106)를 거쳐 수처리된다. 다시 말해, 본 발명의 따른 수처리장치(100)의 주요 구성으로서는, 집수조(101), 탈질미생물의 감소를 완화하기 위한 활성탄접촉여재(10)와 교반기(11)가 부착된 혐기조(102), 투입된 호기성 미생물이 접촉되어 유기물 분해가 이루어질 수 있도록 미생물의 성장환경을 제공함과 동시에 생물막이 형성되도록 하는 비표면적이 대단히 크면서 성형이 자유로운 활성탄접촉여재(10) 및 용존산소농도를 증가시킬 수 있도록 한 산기관(12)이 구비된 폭기조(103), 슬러지(활성오니)를 침전제거할 수 있도록 한 침전조(104), 침전조(104)를 거친 처리수에 용존된 오염물질을 흡착하고 여과하면서 최대한 막힘을 예방할 수 있도록 한 활성탄 여과조(105), 및 여과된 처리수를 소독방류할 수 있는 소독방류조(106)로 이루어지는 것을 특징으로 한다.       Specifically, the constitution of a certain type of water collecting tank 101 is provided so that natural contaminated water containing activated sludge and the like can be collected therein, and the anaerobic tank 102 is a carrier-type activated carbon contact medium according to the present invention. 10 and the stirrer 11, the aeration tank 103 is also equipped with activated carbon contact medium 10 and the diffuser 12 according to the present invention, the precipitation tank 104 in the water passed through the aeration tank 103 The sludge contained in the precipitate is precipitated, and the filter tank 105 is provided with an activated carbon contact medium 10 according to the present invention, and finally, a disinfection discharge tank 106 is provided. The activated carbon contact medium 10 mounted in the anaerobic tank 102 and the aeration tank 103 is preferably a carrier type, and the activated carbon contact medium 10 mounted in the filtration tank 105 is preferably a sheet type. A sludge pump 13 is provided between the settling tank 104 and the filtration tank 105 to send the sludge settled below the settling tank 104 to the anaerobic tank 102 to repeat the water treatment process, and includes little sludge. The treated water is not treated through the filtration tank 105 and the disinfection discharge tank 106. In other words, as the main configuration of the water treatment apparatus 100 according to the present invention, the water collecting tank 101, the anaerobic tank 102 with the activated carbon contact medium 10 and the stirrer 11 to mitigate the reduction of denitrification microorganisms, It provides a growth environment for microorganisms to allow aerobic microorganisms to contact and decompose organic substances, and at the same time, a specific surface area for forming biofilms, and an active carbon contact medium (10) freely molded to increase the dissolved oxygen concentration. The aeration tank 103 equipped with the engine 12, the sedimentation tank 104 for allowing the sludge (activated sludge) to settle and remove the contaminants dissolved in the treated water passed through the sedimentation tank 104, and filtered as much as possible. It is characterized by consisting of an activated carbon filtration tank 105 to prevent, and a disinfection discharge tank 106 that can disinfect and discharge the filtered treated water.

이들의 동작에 대해 설명한다면, 먼저, 활성슬러지 등이 함유된 자연오염수가 집수조(101)에 유입된 후, 상기 집수조(101)에 집수된 오염수는 탈질미생물의 유출을 방지할 수 있도록 활성탄접촉여재(10)가 장착된 혐기조(102)로 유입되고, 상기 혐기조(102)로 유입된 오염처리수는 교반기(11)에 의하여 탈질이 효과적으로 이루어지고 탈질이 이루어진 처리수는 공극과 표면적이 대단히 큰 담체형 활성탄접촉여재(10)에 의해 과부하나 빈부하 등의 충격부하에 견디면서 미생물을 안전하게 성장시킬 수 있는 활성탄접촉여재(10)(담체)가 장착된 폭기조(103)로 이동되면서 안정적으로 유기물을 분해하고, 폭기가 끝난 처리수는 침전조(104)로 이송되어 슬러지가 분리되게 되며, 슬러지를 포함하는 처리수 일부는 슬러지 펌프(13)에 의해 혐기조(102)로 반송되어 다시 탈질을 효과적으로 수행할 수 있도록 구성되어 있다. 그 밖의 슬러지가 분리된 처리수는 최종적으로 시트형 활성탄접촉여재(10)가 장착된 여과조(105)에서 용존된 오염물이 마지막으로 제거된 후 소독방류조(106)를 거쳐 방류되는 동작순서를 따르게 되어 있다.        Referring to the operation of these, first, natural contaminated water containing activated sludge or the like flows into the sump tank 101, and the contaminated water collected in the sump tank 101 is activated carbon contact so as to prevent outflow of denitrification microorganisms. The treated water flowing into the anaerobic tank 102 equipped with the filter medium 10 and introduced into the anaerobic tank 102 is effectively denitrified by the stirrer 11, and the treated water denitrified has a very large void and surface area. Organic materials stably move to the aeration tank 103 equipped with activated carbon contact media 10 (carrier) capable of safely growing microorganisms while enduring impact loads such as overload or poor load by the carrier-type activated carbon contact media 10. And the aerated treated water is transferred to the settling tank 104 to separate the sludge, and a portion of the treated water including the sludge is returned to the anaerobic tank 102 by the sludge pump 13 to be denitrated again. It is configured to perform this effectively. The treated water from which the other sludge is separated follows the operation sequence in which the dissolved contaminants are finally discharged through the disinfection discharge tank 106 after the dissolved contaminants are finally removed from the filtration tank 105 equipped with the sheet-like activated carbon contact medium 10. have.

이와 같이 구성된 본 발명의 비점오염물질 정화용 수처리장치를 이용하여 오염수를 정화하게 되면, 먼저 호기성 미생물들이 접촉되어 생물막을 형성하게 되는 활성탄접촉여재에서 1차적으로 유기물이 분해되고, 유기물 분해가 이루어진 처리수는 다시 한번 활성탄시트를 통과하여 2차적으로 물리적 흡착여과된 상태로 처리되게 되는 것이다.       When the contaminated water is purified using the water treatment apparatus for non-point pollutant purification according to the present invention configured as described above, organic matter is first decomposed in activated carbon contact media, in which aerobic microorganisms are contacted to form a biofilm, and organic matter is decomposed. The water is once again passed through the activated carbon sheet to be treated in a second state of physical adsorption filtration.

상기와 같이 폭기조(103), 침전조(104), 여과조(105)에 각각 본 발명에 따른 담체형 활성탄접촉여재(10)를 내장하여 하나의 시스템으로 단순화함으로써, 담체형 활성탄접촉여재(10)에 형성되는 생물막에 의한 유기물분해와 시트형 활성탄접촉여재(10)에 의한 물리적 여과가 차례로 이루어지고, 그 결과 다양한 고농도 오염수가 고효율로 처리되어 처리용량이 증대되고, 발생되는 슬러지 용량도 50~70% 정도로 감소되며, 시설비 와 운전비 등이 절감되어 경제적인 효과가 매우 우수하다.        As described above, the carrier-type activated carbon contact medium 10 according to the present invention is embedded in the aeration tank 103, the precipitation tank 104, and the filtration tank 105, thereby simplifying the system into the carrier-type activated carbon contact medium 10. Organic decomposition by the formed biofilm and physical filtration by the sheet-like activated carbon contact medium 10 are performed in turn, and as a result, various high concentrations of contaminated water are treated with high efficiency, thereby increasing the treatment capacity and generating sludge capacity of about 50 to 70%. The economic effect is excellent because of the reduction of facility cost and operation cost.

그리고 활성탄접촉여재(10)의 재생시 그대로 활성화하여도 용융된 섬유가 활성탄의 형태를 그대로 유지해주기 때문에 아무런 문제가 발생하지 않는다. 이렇게 만들어진 담체형 활성탄접촉여재는 폭기조내에 장착되어 폭기조내에 투입된 호기성 미생물이 접촉되어 유기물 분해가 이루어질 수 있도록 미생물의 성장환경을 제공함과 동시에 생물막을 폭넓게 형성하며, 활성탄접촉여재 사이사이로 기포를 부상시킬 수 있도록 에어를 강제 공급하여 용존산소농도를 증가시킬 수 있도록 하는 산기관을 포함함으로써 폭기효과를 높일 수 있다.       And even when activated as the regeneration of the activated carbon contact medium 10 does not cause any problem because the molten fibers maintain the form of the activated carbon as it is. Carrier-type activated carbon contact media made in this way is provided in the aeration tank to provide a growth environment for microorganisms to contact organic aerobic microorganisms introduced into the aeration tank, and to form a wide biofilm, and to inflate bubbles between activated carbon contact media. The aeration effect can be enhanced by including an air inlet that can force air to increase the dissolved oxygen concentration.

이상과 같이 본 발명을 실시예를 참고하여 설명하였으나, 이는 본 발명을 설명하기 위한 것일 뿐이며, 본 발명이 속하는 기술 분야의 통상의 식을 가진 자라면 발명의 상세한 설명으로부터 다양한 변형 또는 균등한 실시예가 가능하다는 것을 이해할 수 있을 것이다. 따라서 본 발명의 진정한 권리범위는 특허청구범위의 기술적 사상에 의해 결정되어야 할 것이다.        Although the present invention has been described with reference to the embodiments, it is only for the purpose of illustrating the present invention, and various modifications or equivalent embodiments of the present invention will be apparent to those having ordinary skill in the art to which the present invention pertains. You will understand that it is possible. Accordingly, the true scope of the present invention should be determined by the technical idea of the claims.

1: 활성탄 입자 2: 섬유재
3: 접착성 수지 10: 활성탄접촉여재
11: 교반기 12: 산기관
13: 슬러지 펌프 101: 집수조
102: 혐기조 103: 폭기조
104: 침전조 105: 여과조
106: 소독방류조
1: activated carbon particle 2: fiber material
3: adhesive resin 10: activated carbon contact media
11: stirrer 12: diffuser
13: sludge pump 101: sump
102: anaerobic tank 103: aeration tank
104: sedimentation tank 105: filtration tank
106: Disinfection Discharge Tank

Claims (15)

부직포 형태의 제1섬유재;
상기 제1섬유재 상에 분사된 제1접착성 수지;
상기 제1접착성 수지 상에 살포된 활성탄 입자;
상기 활성탄 입자 위에 적층된 부직포 형태의 제2섬유재;
상기 제2섬유재 상에 분사된 제2접착성 수지를 포함하여 구성되며,
상기 제1섬유재와 제1접착성 수지, 활성탄 입자, 제2섬유재 및 제2접착성 수지는 압력을 가하여 접착된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
A first fibrous material in the form of a nonwoven fabric;
A first adhesive resin sprayed on the first fiber material;
Activated carbon particles sprayed on the first adhesive resin;
A second fibrous material in the form of a nonwoven fabric laminated on the activated carbon particles;
It is configured to include a second adhesive resin sprayed on the second fiber material,
The first carbon material and the first adhesive resin, activated carbon particles, the second fiber material and the second adhesive resin is activated carbon contact filter for organic material adsorption decomposition, characterized in that the adhesive is applied under pressure.
제1항에 있어서,
상기 제1섬유재 및 제2섬유재는 폴리에테르 또는 폴리에스테르인 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The first fiber material and the second fiber material is activated carbon contact media for adsorptive decomposition of organic matters, characterized in that the polyether or polyester.
제1항에 있어서,
상기 접착성 수지는 아크릴, 에폭시, 초산비닐, PVC 재질 중 어느 하나인 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The adhesive resin is activated carbon contact media for organic material adsorption decomposition, characterized in that any one of acrylic, epoxy, vinyl acetate, PVC material.
제1항에 있어서,
상기 활성탄접촉여재는,
모형에 의해 담체형 또는 시트형으로 형성된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The activated carbon contact media,
Activated carbon contact medium for adsorptive decomposition of organic matters, characterized in that formed in a carrier or sheet form by a model.
제1항에 있어서,
상기 제1 및 제2섬유재는 중량 50g/m2으로 평평히 깔고, 상기 제1 및 제2접착성 수지는 중량 10g/m2으로 분사되며, 상기 활성탄 입자는 중량 100g/m2으로 살포되는 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The first and the second fiber material is laid flat with a weight of 50g / m 2 , the first and second adhesive resin is sprayed with a weight of 10g / m 2 , the activated carbon particles are sprayed at a weight of 100g / m 2 Activated carbon contact medium for adsorptive decomposition of organic matters.
제1항에 있어서,
상기 활성탄 접촉여재는 모형 속에서 150℃의 온도로 성형된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The activated carbon contact medium is activated carbon contact medium for adsorption decomposition of organic material, characterized in that molded at a temperature of 150 ℃ in the model.
제1항에 있어서,
상기 제1섬유재, 제1접착성 수지, 활성탄 입자, 제2섬유재 및 제2접착성 수지를 반복하여 적층시킨 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
Activated carbon contact filter medium for adsorptive decomposition of organic matters, characterized in that the first fiber material, the first adhesive resin, activated carbon particles, the second fiber material and the second adhesive resin are laminated repeatedly.
제1항에 있어서,
상기 제1섬유재 및 제2섬유재는 고온 용해성 섬유재와 저온 용해성 섬유재가 혼합된 부직포로 형성되며,
상기 제1섬유재와 제2섬유재, 제1접착성 수지, 활성탄 입자 및 제2접착성 수지는 모형 속에서 열과 압력을 가하여 접착된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
The method of claim 1,
The first fiber material and the second fiber material is formed of a nonwoven fabric mixed with a high temperature soluble fiber material and a low temperature soluble fiber material,
The first carbon material and the second fiber material, the first adhesive resin, activated carbon particles and the second adhesive resin is activated carbon contact filter for organic material adsorption decomposition, characterized in that bonded by applying heat and pressure in the model.
제8항에 있어서,
상기 저온 용해성 섬유재는 폴리에테르이고, 상기 고온 용해성 섬유재는 폴리에스테르인 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
9. The method of claim 8,
The low temperature soluble fiber material is a polyether, and the high temperature soluble fiber material is an active carbon contact medium for adsorption decomposition of organic material, characterized in that the polyester.
제8항에 있어서,
상기 활성탄접촉여재는 100 내지 200℃의 온도에서 성형된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
9. The method of claim 8,
The activated carbon contact media for activated carbon contact media for organic material adsorption decomposition, characterized in that molded at a temperature of 100 to 200 ℃.
제8항에 있어서,
상기 제1섬유재, 제1접착성 수지, 활성탄 입자, 제2섬유재 및 제2접착성 수지를 반복하여 적층시킨 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
9. The method of claim 8,
Activated carbon contact filter medium for adsorptive decomposition of organic matters, characterized in that the first fiber material, the first adhesive resin, activated carbon particles, the second fiber material and the second adhesive resin are laminated repeatedly.
제8항에 있어서,
상기 제1 섬유재와 제2 섬유재는 저온 용해성 섬유재 중량 20g/m2, 상기 고온 용해성 섬유재 중량 50g/m2을 혼합하여 평평히 깔고, 상기 제1 및 제2접착성 수지는 중량 10g/m2으로 분사하며, 상기 활성탄 입자는 중량 100g/m2으로 살포된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
9. The method of claim 8,
The first fiber and the second fiber is laid flat and mixed with a low temperature soluble fiber weight 20g / m 2 , the weight of the high temperature soluble fiber 50g / m 2 , the first and second adhesive resin weight 10g / injected in m 2, and the activated carbon particles adsorb organic matter decomposition activated carbon filter material for contact, characterized in that the spraying on a weight 100g / m 2.
제8항에 있어서,
상기 활성탄접촉여재는,
상기 모형에 의해 담체형 또는 시트형으로 형성된 것을 특징으로 하는 유기물 흡착분해용 활성탄접촉여재.
9. The method of claim 8,
The activated carbon contact media,
Activated carbon contact medium for adsorptive decomposition of organic matters, characterized in that formed in a carrier or sheet form by the model.
집수조, 혐기조, 폭기조, 침전조, 여과조, 소독방류조를 포함하여 구성된 비점오염물질 정화용 수처리장치에 있어서,
상기 혐기조, 폭기조 및 여과조 내에는 제1항 내지 제13항 중 어느 한 항에 기재된 유기물 흡착분해용 활성탄접촉여재가 장착된 것을 특징으로 하는 비점오염물질 정화용 수처리장치.
In the water treatment apparatus for purification of non-point pollutants, including a collecting tank, anaerobic tank, aeration tank, sedimentation tank, filtration tank, and disinfection tank,
14. An apparatus for purifying non-point pollutants, wherein the anaerobic tank, aeration tank and filtration tank are equipped with activated carbon contact media for adsorption and decomposition of organic matter according to any one of claims 1 to 13.
제14항에 있어서,
상기 혐기조 및 폭기조 내에 장착되는 유기물 흡착분해용 활성탄접촉여재의 형상은 담체형이고, 상기 여과조 내에 장착되는 유기물 흡착분해용 활성탄접촉여재의 형상은 시트형으로 형성된 것을 특징으로 하는 비점오염물질 정화용 수처리장치.
15. The method of claim 14,
The shape of the activated carbon contact medium for adsorption decomposition of organic matter mounted in the anaerobic tank and the aeration tank is a carrier type, the shape of the activated carbon contact medium for adsorption decomposition of organic matter mounted in the filtration tank is formed of a sheet-like water treatment device for purification of non-point pollutants.
KR1020110013275A 2011-02-15 2011-02-15 Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same KR101278101B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020110013275A KR101278101B1 (en) 2011-02-15 2011-02-15 Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020110013275A KR101278101B1 (en) 2011-02-15 2011-02-15 Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same

Publications (2)

Publication Number Publication Date
KR20120093610A KR20120093610A (en) 2012-08-23
KR101278101B1 true KR101278101B1 (en) 2013-06-24

Family

ID=46884976

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020110013275A KR101278101B1 (en) 2011-02-15 2011-02-15 Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same

Country Status (1)

Country Link
KR (1) KR101278101B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102139052B1 (en) * 2019-01-02 2020-07-29 한국과학기술연구원 Aquifer storage and recovery system including aerobic reactor using microbes from underground aquifer

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0923881A (en) * 1995-07-13 1997-01-28 Toray Ind Inc Microorganism carrier, its production and biological treating apparatus using the carrier
JPH1076250A (en) * 1996-09-06 1998-03-24 Unitika Ltd Adsorbent and water treatment method using the same
KR20010088735A (en) * 2001-08-28 2001-09-28 양금모 A method for manufacturing density-controlled tube-chip type biocarriers and the biocarriers manufactured thereby
KR20030066880A (en) * 2002-02-05 2003-08-14 곽종운 A microorganism media and method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0923881A (en) * 1995-07-13 1997-01-28 Toray Ind Inc Microorganism carrier, its production and biological treating apparatus using the carrier
JPH1076250A (en) * 1996-09-06 1998-03-24 Unitika Ltd Adsorbent and water treatment method using the same
KR20010088735A (en) * 2001-08-28 2001-09-28 양금모 A method for manufacturing density-controlled tube-chip type biocarriers and the biocarriers manufactured thereby
KR20030066880A (en) * 2002-02-05 2003-08-14 곽종운 A microorganism media and method thereof

Also Published As

Publication number Publication date
KR20120093610A (en) 2012-08-23

Similar Documents

Publication Publication Date Title
CN100558659C (en) The method of circulating water culture system water treatment
KR101909098B1 (en) Spherical bodies having contact oxidation function and manufacturing method
KR100726353B1 (en) The composite reactivity clean apparatus of dirty and waste water and the cleaning method thereof
CN105813988A (en) Method for biological purification of water
KR100827641B1 (en) Contact oxidation tank for waste water treatment
KR20070037721A (en) The water treatment facilities with the function of dissolved air flotation, filtration, membrane-separation and biofilter
CN208545256U (en) A kind of artificial wet land system handling fluoride waste
JPH0871414A (en) Fluid treating agent composition
CN109020071A (en) A kind of sewage three is in contact biological treatment and integrated apparatus system
CN206607121U (en) Biological activated carbon absorption, degraded, filtering integral equipment
KR100961452B1 (en) Biological filtration device for water treatment and waste water treatment
KR101278101B1 (en) Activated carbon-contact media for adsorbing and resolving organic matter and water treatment system for purifying non-point source of contaminant using the same
KR102287700B1 (en) Water treatment system of artificial wetland
CN203065308U (en) Wetland sewage treatment system
KR20130032137A (en) An activated carbon watertreatment device and the watertreatment system and the method using thereof
KR101330207B1 (en) Activated absorption member, method of manufacturing the same, apparatus and method for water treatment using the activated absorption member
CN106698677A (en) Water treatment purifier and water treatment method thereof
KR101220228B1 (en) Water Treatment Facilities
KR101670728B1 (en) Apparatus for water treatment combined vehicle using activated carbon fiber
CN104118941A (en) Efficient nitrogen and phosphorus removal artificial wetland device
KR100436981B1 (en) Water-treatment apparatus
KR100552098B1 (en) Dual-compressible synthetic media filter and secondary effluent reclamation system using the same
KR100991970B1 (en) Advanced treatment process moving bio-media
KR100636617B1 (en) The composite reactivity clean apparatus of dirty and waste water and the cleaning method thereof
CN105585158B (en) A kind of multi-functional curtain of purification of water quality

Legal Events

Date Code Title Description
A201 Request for examination
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20160525

Year of fee payment: 4

FPAY Annual fee payment

Payment date: 20170526

Year of fee payment: 5

FPAY Annual fee payment

Payment date: 20180525

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20190527

Year of fee payment: 7