KR102497137B1 - Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency - Google Patents

Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency Download PDF

Info

Publication number
KR102497137B1
KR102497137B1 KR1020210113540A KR20210113540A KR102497137B1 KR 102497137 B1 KR102497137 B1 KR 102497137B1 KR 1020210113540 A KR1020210113540 A KR 1020210113540A KR 20210113540 A KR20210113540 A KR 20210113540A KR 102497137 B1 KR102497137 B1 KR 102497137B1
Authority
KR
South Korea
Prior art keywords
tank
water
treated
filter
flotation
Prior art date
Application number
KR1020210113540A
Other languages
Korean (ko)
Inventor
정래화
서진용
김병선
서현우
Original Assignee
(주)동명기술공단종합건축사사무소
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 (주)동명기술공단종합건축사사무소 filed Critical (주)동명기술공단종합건축사사무소
Priority to KR1020210113540A priority Critical patent/KR102497137B1/en
Application granted granted Critical
Publication of KR102497137B1 publication Critical patent/KR102497137B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/28Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed moving during the filtration
    • B01D24/30Translation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46Regenerating the filtering material in the filter
    • B01D24/4668Regenerating the filtering material in the filter by moving the filtering element
    • B01D24/4673Regenerating the filtering material in the filter by moving the filtering element using rotary devices or vibration mechanisms, e.g. stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46Regenerating the filtering material in the filter
    • B01D24/4694Regenerating the filtering material in the filter containing filter material retaining means (e.g. screens, balls) placed on the surface of the filter material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23121Diffusers having injection means, e.g. nozzles with circumferential outlet
    • 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
    • C02F1/008Control or steering systems not provided for elsewhere in subclass C02F
    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • 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
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • 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
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • 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
    • C02F3/12Activated sludge processes
    • C02F3/1205Particular type of activated sludge processes
    • C02F3/1215Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
    • 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
    • C02F3/30Aerobic and anaerobic processes
    • 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

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Physical Water Treatments (AREA)

Abstract

The present invention provides an advanced sewage treatment apparatus comprising a floating filtration tank having improved treatment efficiency, which comprises: a flow rate control tank (1); an anaerobic tank (2) removing phosphorus in treated water introduced from the flow rate control tank (1); an anoxic tank (3) removing nitrate nitrogen in the treated water introduced from the anaerobic tank (2); an aerobic tank (4) aerating air into the treated water introduced from the anoxic tank (3) to nitrify nitrogen; a sedimentation tank (5) separating the treated water introduced from the aerobic tank (4) into supernatant and sludge; a high-temperature sterilization unit (200) sterilizing the treated water at high temperature by heat exchange; and a floating filtration tank (100), wherein the high-temperature sterilization unit (200) is installed on the front end of the floating filtration tank and consists of an inner pipe (210) through which the treated water is transported and an outer pipe (220) that surrounds the inner pipe (210) and supplies high-temperature heat to the treated water in the inner pipe by allowing a high-temperature heat medium to flow therethrough.

Description

처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치{ADVANCED WASTEWATER TREATMENT APPARATUS COMPRISING FLOATING FILTER TANK WITH IMPROVED TREATING EFFICIENCY}Advanced sewage treatment system including floating filter tank with improved treatment efficiency

본 발명은 하수고도처리장치에 관한 것으로, 보다 상세하게는 C/N비가 낮은 폐수의 유기물 및 영양염류(질소 및 인)를 신속하고 효과적으로 처리하여 폐수를 정화시키고, 폐수처리 시설의 설치면적을 줄이고 운전·관리를 손쉽게 할 수 있는 처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치에 관한 것이다.The present invention relates to an advanced sewage treatment system, and more particularly, to rapidly and effectively treat organic matter and nutrients (nitrogen and phosphorus) in wastewater with a low C/N ratio, to purify wastewater, and to reduce the installation area of wastewater treatment facilities. It relates to an advanced sewage treatment system including a flotation filter with improved treatment efficiency that can be easily operated and managed.

최근 들어, 도시하수, 마을하수도 및 오ㅇ폐수의 영양염류에 의한 하천이나, 연안바다 및 호소(호수 및 저수지)등의 부영양화가 심각함에 따라 이에 대한 대책으로 영양염류의 처리가 필요하다.Recently, as the eutrophication of rivers, coastal seas and lakes (lakes and reservoirs) caused by nutrient salts of urban sewage, village sewage, and wastewater is serious, it is necessary to treat nutrient salts as a countermeasure against this.

폐수 중 질소 및 인을 제거하기 위한 방법으로는 물리ㅇ화학적 방법 및 생물학적 방법으로 나누어 볼 수 있다. 물리ㅇ화학적 방법은 처리시설 및 화학약품을 이용함으로써 경제적인 비용이 많이 소요된다.Methods for removing nitrogen and phosphorus from wastewater can be divided into physical and chemical methods and biological methods. Physical and chemical methods require a lot of economic cost by using treatment facilities and chemicals.

따라서 경제적인 미생물을 이용한 생물학적처리 방법이 많이 개발되었다. 하지만 이런 생물학적처리 방법들은 C/N비가 낮은 국내 폐수처리시 체류시간, 부지면적, 질소ㅇ인 처리효율 및 유입 부하변동에 대처 능력 등을 해결하는데 많은 어려움을 지니고 있다.Therefore, many biological treatment methods using economical microorganisms have been developed. However, these biological treatment methods have many difficulties in solving residence time, site area, nitrogen treatment efficiency, and ability to cope with inflow load fluctuations in domestic wastewater treatment with a low C/N ratio.

이들 문제점을 해결하기 위하여 기존의 질소ㅇ인 처리공정(바덴포, A 2 /O, UCT 및 VIP등)의 변법 및 메디아를 이용한 공정이 개발되고 있다. 메디아를 이용한 질소ㅇ인 처리공정은 메디아에 부착된 고농도의 미생물을 이용함으로써 폐수처리시 체류시간 단축, 설치면적의 축소 및 슬러지 발생량을 감소시킬 수 있다. 특히, 부상여재를 이용한 처리공정은 여재의 단가가 저렴하여 다른 유동상 메디아 및 고정상 메디아보다 큰 장점을 가지고 있으며 생물학적 분해작용과 물리적인 여과작용이 동시에 이루어져 안정적인 처리수질을 이룰 수 있다.In order to solve these problems, a modification of the existing nitrogen ㅇ phosphorus treatment process (Badenpo, A 2 /O, UCT and VIP, etc.) and a process using media are being developed. Nitrogen treatment process using media can shorten residence time, reduce installation area, and reduce sludge generation during wastewater treatment by using high-concentration microorganisms attached to media. In particular, the treatment process using flotation media has a great advantage over other fluidized bed media and fixed bed media because the unit price of the media is low, and stable treatment water quality can be achieved through biological degradation and physical filtration at the same time.

부상여재를 이용한 처리시설의 운영에 있어서 가장 중요한 것은 역세방식이다. 현재 역세방식은 공기, 물 및 프로펠러를 이용한 역세가 이루어진다. 공기를 이용한 역세방식은 브로와 및 컴프레셔에 의해 고압으로 주입하여 줌으로써 동력비가 많이 소요되며 역세시 물에 의한 역세 방식은 물량이 과량으로 소비되는 단점이 있다. 이들 공기 또는 물을 이용한 역세방식은 여재의 팽창으로 인한 하부 공간을 넓게 확보하여야 한다. 또한, 프로펠러에 의한 역세방식은 일반적으로 물과 함께 이용되는데 동력비가 많이 소요된다.The most important thing in the operation of treatment facilities using flotation media is the backwash method. The current backwashing method consists of backwashing using air, water and a propeller. The backwashing method using air requires a lot of power costs because it is injected at high pressure by a blower and a compressor, and the backwashing method using water during backwashing has a disadvantage in that an excessive amount of water is consumed. In the backwashing method using air or water, a wide lower space due to the expansion of the filter medium must be secured. In addition, the backwashing method by the propeller is generally used with water, but it requires a lot of power cost.

일반적으로, 부상여재를 이용한 처리시설은 유기물 및 부유물질을 제거하기 위한 처리시설이며 질소 및 인은 미생물의 동화작용에 의해 제거되는 수준인 20 ∼ 30%에 불과하다. 따라서 부상여재를 이용한 유기물, 질소 및 인의 처리시설은 아직 미흡한 상태이다. 나아가 부상여재를 포함한 여과조내의 실시간 상태를 확인할 수 없어 제때 적절한 상황별 조치를 강구하기 어려워 처리효율을 저하하는 문제가 대두되고 있다.In general, a treatment facility using flotation media is a treatment facility for removing organic matter and suspended matter, and only 20 to 30% of nitrogen and phosphorus is removed by the assimilation of microorganisms. Therefore, treatment facilities for organic matter, nitrogen and phosphorus using flotation media are still insufficient. Furthermore, since it is impossible to check real-time conditions in the filtration tank, including the floating filter media, it is difficult to devise appropriate measures for each situation in time, resulting in a problem of lowering treatment efficiency.

본 발명의 목적은 C/N비가 낮은 폐수의 유기물 및 영양염류(질소 및 인)를 신속하고 효과적으로 처리하여 폐수를 정화시키고, 폐수처리 시설의 설치면적을 줄이고 운전ㅇ관리를 손쉽게 할 수 있도록 해주는 처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치를 제공하는 데에 있다.An object of the present invention is to quickly and effectively treat organic matter and nutrients (nitrogen and phosphorus) of wastewater with a low C/N ratio to purify wastewater, reduce the installation area of wastewater treatment facilities, and facilitate operation and management. It is an object of the present invention to provide an advanced sewage treatment system including a flotation filter with improved efficiency.

상기한 바와 같은 본 발명의 기술적 과제는 다음과 같은 수단에 의해 달성되어진다.The technical problem of the present invention as described above is achieved by the following means.

(1) 유량조정조; 유량조정조로부터 유입되는 피처리수 중의 인을 제거하는 혐기조; 상기 혐기조로부터 유입되는 피처리수 중의 질산성 질소를 제거하는 무산소조; 상기 무산소조로부터 유입되는 피처리수 중으로 공기를 폭기시켜 질소를 질산화시키는 호기조; 상기 호기조로부터 유입되는 피처리수를 상등액과 슬러지로 분리시키는 침전조; 열교환에 의해 피처리수를 소온살균처리하는 고온살균부; 및 부상여과조를 포함하되,(1) flow control tank; an anaerobic tank for removing phosphorus in the water to be treated flowing in from the flow control tank; an anoxic tank for removing nitrate nitrogen from the water to be treated flowing in from the anaerobic tank; an aerobic tank for nitrifying nitrogen by aerating air into the water to be treated flowing from the anoxic tank; a sedimentation tank which separates the water to be treated from the aerobic tank into supernatant and sludge; a high-temperature sterilization unit that sterilizes the water to be treated by heat exchange; And including a flotation filtration tank,

상기 고온살균부는 부상여과조 전단에 설치되며, 피처리수가 이송되는 내관, 및 상기 내관을 둘러싸고 내부에 고온의 열매체가 흘러 상기 내관의 피처리수에 고온의 열을 공급하는 외관으로 이루어진 것을 특징으로 하는 처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치.The high-temperature sterilization unit is installed at the front end of the flotation filtration tank, and consists of an inner tube through which the water to be treated is transported, and an exterior that surrounds the inner tube and supplies high-temperature heat to the water to be treated in the inner tube by flowing a high-temperature heat medium inside the inner tube. An advanced sewage treatment system including a flotation filter with improved treatment efficiency.

(2) 상기 (1)에서, 부상여과조는, (2) In the above (1), the floating filter tank,

피처리수가 유입되는 유입부, 피처리수 유입공간에 장착되는 부상여과장치, 및 피처리수가 배출되는 배출부를 포함하되,Including an inlet through which the water to be treated flows in, a flotation filtration device installed in the inflow space of the water to be treated, and an outlet through which the water to be treated is discharged,

상기 부상여과장치는,The floating filter device,

저면에 장착된 유입여과망 및 상단 일측에 장착된 배출여과망을 갖고 내부에 부상여재를 수용하여 피처리수를 여과처리하는 여과탱크; 상기 여과탱크내 수용되며 피처리수와 함께 부상하면서 오염물질을 제거하는 부상여재; 여과탱크내 상부 제1측에 장착되어, 반대편인 제2측으로 피처리수를 이동시키는 제1프로펠러; 여과탱크내 하부 제2측에 장착되어, 반대편인 제1측으로 피처리수를 이동시키는 제2프로펠러; 여과탱크내 하부 제1측에 장착되어 상기 제2프로펠러에 의해 이동된 피처리수와 함께 이동되는 부상여재에 초음파를 방사하는 초음파발진기; 및 여과탱크내 제2측 벽면과 이격되어 형성되어, 피처리수와 부상여재를 하방으로 순환시키도록 가이드하는 가이드격벽을 포함하는 것을 특징으로 하는 처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치.A filter tank having an inlet filter net attached to the bottom and a discharge filter net attached to one side of the top, and accommodating the flotation filter medium therein to filter the water to be treated; a flotation filter medium accommodated in the filtration tank and removing contaminants while floating together with the water to be treated; A first propeller mounted on a first side of the upper part of the filter tank to move the water to be treated to a second side opposite to the first side; a second propeller mounted on a lower second side of the filtration tank to move the water to be treated to the opposite first side; an ultrasonic generator mounted on a lower first side of the filter tank and radiating ultrasonic waves to the floating filter media moving together with the water to be treated moved by the second propeller; and a guide bulkhead formed to be spaced apart from the second side wall of the filtration tank and guiding the water to be treated and the flotation media to circulate downward. Device.

(3) 상기 (2)에 있어서,(3) In the above (2),

상기 제1프로펠러, 제2프로펠러, 및 초음파발진기는 측벽 내부 수용부에 수납되어지는 것을 특징으로 하는 실시간 모니터링이 가능한 부상여과조를 포함하는 하수고도처리장치.The first propeller, the second propeller, and the ultrasonic generator are housed in the inner accommodating part of the side wall.

(4) 상기 (2)에 있어서,(4) In the above (2),

가이드격벽의 내부에 수직방향으로 적어도 1 이상의 산소공급부가 장착되며, 상기 산소공급부는 산소공급관과 산소공급노즐로 구성되어 하강하는 부상여재와 피처리수에 함유된 오염물질을 제거하는 것을 특징으로 하는 하수고도처리장치.At least one oxygen supply unit is mounted in the vertical direction inside the guide bulkhead, and the oxygen supply unit is composed of an oxygen supply pipe and an oxygen supply nozzle, and removes contaminants contained in the floating filter medium and the water to be treated. Sewage advanced treatment system.

본 발명에 의하면, C/N비가 낮은 폐수의 유기물 및 영양염류(질소 및 인)를 신속하고 효과적으로 처리하여 폐수를 정화시키고, 폐수처리 시설의 설치면적을 줄이고 운전ㅇ관리를 손쉽게 할 수 있도록 해주는 효과를 제공한다.According to the present invention, the organic matter and nutrients (nitrogen and phosphorus) of wastewater with a low C/N ratio are quickly and effectively treated to purify wastewater, reduce the installation area of wastewater treatment facilities, and facilitate operation and management. provides

도 1은 본 발명에 따른 하수고도처리장치의 전체 구성도.
도 2는 본 발명에 따른 고온살균부 및 부상여과조의 구성도.
도 3은 본 발명에 따른 부상여과장치의 세부 구성도.
1 is an overall configuration diagram of an advanced sewage treatment system according to the present invention.
Figure 2 is a configuration diagram of a high-temperature sterilization unit and flotation filtration tank according to the present invention.
Figure 3 is a detailed configuration of the flotation filter device according to the present invention.

이하, 본 발명에 따른 바람직한 실시 형태를 첨부된 도면을 참조하여 상세하게 설명한다. 첨부된 도면과 함께 이하에 개시될 상세한 설명은 본 발명의 예시적인 실시형태를 설명하고자 하는 것이며, 본 발명이 실시될 수 있는 유일한 실시형태를 나타내고자 하는 것이 아니다. 이하의 상세한 설명은 본 발명의 완전한 이해를 제공하기 위해서 구체적 세부사항을 포함한다. 그러나, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자는 본 발명이 이러한 구체적 세부사항 없이도 실시될 수 있음을 안다.Hereinafter, preferred embodiments according to the present invention will be described in detail with reference to the accompanying drawings. The detailed description set forth below in conjunction with the accompanying drawings is intended to describe exemplary embodiments of the present invention and is not intended to represent the only embodiments in which the present invention may be practiced. The following detailed description includes specific details for the purpose of providing a thorough understanding of the present invention. However, one of ordinary skill in the art to which this invention pertains knows that the invention may be practiced without these specific details.

몇몇 경우, 본 발명의 개념이 모호해지는 것을 피하기 위하여 공지의 구조 및 장치는 생략되거나, 각 구조 및 장치의 핵심기능을 중심으로 한 블록도 형식으로 도시될 수 있다.In some cases, in order to avoid obscuring the concept of the present invention, well-known structures and devices may be omitted or may be shown in block diagram form centering on core functions of each structure and device.

명세서 전체에서, 어떤 부분이 어떤 구성요소를 "포함(comprising 또는 including)"한다고 할 때, 이는 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 포함할 수 있는 것을 의미한다. 또한, 명세서에 기재된 "…부"의 용어는 적어도 하나의 기능이나 동작을 처리하는 단위를 의미한다. 또한, "일(a 또는 an)", "하나(one)", "그(the)" 및 유사 관련어는 본 발명을 기술하는 문맥에 있어서(특히, 이하의 청구항의 문맥에서) 본 명세서에 달리 지시되거나 문맥에 의해 분명하게 반박되지 않는 한, 단수 및 복수 모두를 포함하는 의미로 사용될 수 있다.Throughout the specification, when a part is said to "comprising" or "including" a certain element, it means that it may further include other elements, not excluding other elements, unless otherwise stated. do. Also, the term "... unit" described in the specification means a unit that processes at least one function or operation. Also, "a or an", "one", "the" and similar related words in the context of describing the invention (particularly in the context of the claims below) Unless indicated or otherwise clearly contradicted by context, both the singular and the plural can be used.

본 발명의 실시예들을 설명함에 있어서 공지 기능 또는 구성에 대한 구체적인 설명이 본 발명의 요지를 불필요하게 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명을 생략할 것이다. 그리고 후술되는 용어들은 본 발명의 실시예에서의 기능을 고려하여 정의된 용어들로서 이는 사용자, 운용자의 의도 또는 관례 등에 따라 달라질 수 있다. 그러므로 그 정의는 본 명세서 전반에 걸친 내용을 토대로 내려져야 할 것이다.In describing the embodiments of the present invention, if it is determined that a detailed description of a known function or configuration may unnecessarily obscure the subject matter of the present invention, the detailed description will be omitted. In addition, terms to be described later are terms defined in consideration of functions in the embodiment of the present invention, which may vary according to the intention or custom of a user or operator. Therefore, the definition should be made based on the contents throughout this specification.

이하, 본 발명의 바람직한 실시 예를 첨부된 도면을 참조하여 설명한다.Hereinafter, preferred embodiments of the present invention will be described with reference to the accompanying drawings.

본 발명의 하수고도처리장치는 도 1에 도시한 바와 같이, 유량조정조(1)로부터 유입되는 피처리수 중의 인을 제거하는 혐기조(2), 상기 혐기조(2)로부터 유입되는 피처리수 중의 질산성 질소를 제거하는 무산소조(3), 상기 무산소조(3)로부터 유입되는 피처리수 중으로 공기를 폭기시켜 질소를 질산화시키는 호기조(4), 상기 호기조(4)로부터 유입되는 피처리수를 상등액과 슬러지로 분리시키는 침전조(5), 열교환에 의해 상기 상등액을 고온살균처리하는 고온살균부(200) 및 부상여과조(100)를 포함한다.As shown in FIG. 1, the advanced sewage treatment system of the present invention is an anaerobic tank (2) for removing phosphorus in the water to be treated flowing in from the flow control tank (1), and the quality of the water to be treated flowing in from the anaerobic tank (2) An anoxic tank (3) for removing acidic nitrogen, an aerobic tank (4) for nitrifying nitrogen by aerating air into the treated water flowing from the anoxic tank (3), and treating the treated water flowing from the aerobic tank (4) as supernatant and sludge It includes a sedimentation tank 5 for separating into, a high-temperature sterilization unit 200 for high-temperature sterilization of the supernatant by heat exchange, and a flotation filter tank 100.

본 발명에서는 상기 고온살균부(200) 및 부상여과조(100)를 제외한 장치 구성은 공지의 것을 그대로 이용하여도 무방하다. 이하 고온살균부 및 부상여과조를 중점하여 설명하기로 하고, 이외의 구체적인 장치구성에 대한 상세한 설명은 생략하기로 한다.In the present invention, the device configuration except for the high-temperature sterilization unit 200 and the flotation filter tank 100 may be used as it is. Hereinafter, the high-temperature sterilization unit and the flotation filtration tank will be described with emphasis, and detailed descriptions of other specific device configurations will be omitted.

도 2에 도시한 바와 같이, 본 발명에 따른 상기 고온살균부(200)는 부상여과조(100) 전단에 설치되며, 피처리수가 이송되는 내관(210), 및 상기 내관(220)을 둘러싸고 내부에 고온의 열매체가 흘러 상기 내관의 피처리수에 고온의 열을 공급하는 외관(220)으로 이루어진다.As shown in FIG. 2, the high-temperature sterilization unit 200 according to the present invention is installed at the front end of the flotation filtration tank 100, surrounds the inner tube 210 through which the water to be treated is transported, and the inner tube 220, and inside It consists of an outer tube 220 in which a high-temperature heat medium flows and supplies high-temperature heat to the water to be treated in the inner tube.

상기 열매체는 고온의 스팀일 수 있으며, 외부 스팀공급장치(미도시)를 통해 외관(220)과 내관의 사이공간에 투입되어 흐르게 한다. 내관(210)은 침전조(5)로부터 분리된 상등액이 이송되는 관으로 상기 외관내 흐르는 열매체에 의해 열을 공급받아 각종 유기물의 분해를 촉진함과 동시에 미생물을 살균하는 효과를 제공한다.The heating medium may be high-temperature steam, and is injected into the space between the outer tube 220 and the inner tube through an external steam supply device (not shown) to flow. The inner tube 210 is a tube through which the supernatant liquid separated from the settling tank 5 is transported. Heat is supplied by a heat medium flowing inside the outer tube to promote the decomposition of various organic substances and at the same time provide an effect of sterilizing microorganisms.

본 발명에 따른 하수고도처리장치는 도 2에 도시한 바와 같이 말단에 부상여과조(100)를 포함하고, 상기 부상여과조(100)는 유입부(110), 유입공간부(140) 내 장착된 부상여과장치(120), 및 배출부(130)를 포함한다.As shown in FIG. 2, the advanced sewage treatment apparatus according to the present invention includes a flotation filter tank 100 at the end, and the flotation filter tank 100 is mounted in the inlet part 110 and the inlet space part 140. It includes a filtering device 120 and a discharge unit 130.

본 발명에서 상기 부상여과장치(120)의 상부에는 카메라부(150)가 설치된다. 상기 카메라부(150)는 부상여과장치(120)의 투명상판(13)의 상면을 촬영하는 것으로 통상적인 감시카메라일 수 있다.In the present invention, a camera unit 150 is installed on the top of the flotation filter 120. The camera unit 150 may be a conventional surveillance camera that photographs the upper surface of the transparent top plate 13 of the flotation filter 120.

바람직하게는 상기 부상여과장치(120)의 하부에는 미세기포공급부(160,161)가 장착된다. 미세기포공급부는 미세기포 공급관(160)과 미세기포 공급노즐(161)을 포함하며, 도시되지 않았으나 상기 미세기포 공급관(160)은 외부 미세기포발생기와 연결되어 미세기포를 공급받는다.Preferably, micro-bubble supply units 160 and 161 are mounted on the lower portion of the flotation filter 120. The micro-bubble supply unit includes a micro-bubble supply pipe 160 and a micro-bubble supply nozzle 161. Although not shown, the micro-bubble supply pipe 160 is connected to an external micro-bubble generator to receive micro-bubbles.

미세기포가 부상여과장치(120)의 하면을 이루는 유입여과망(11) 위로 미세기포를 공급하면, 상기 미세기포는 피처리수내 함유된 오염물질의 확산을 촉진시켜 부상여재(20)과의 접촉효율을 증진시킨다.When the microbubbles are supplied onto the inlet filter net 11 constituting the lower surface of the flotation filter device 120, the microbubbles promote the diffusion of contaminants contained in the water to be treated, thereby increasing the contact efficiency with the flotation filter medium 20. promote

상승하는 미세기포는 투명상판(13)에서 정상적으로 작동할 경우 소정의 패턴을 형성하게 되는데 정상적으로 작동할 수 없는 상황(예로, 부상여재가 서로 응집되거나 이동이 잘 이루어지지 않는 상황)에서는 패턴이 잘 관찰되지 않게 된다. 카메라부(150)는 이러한 패턴을 실시간 감시하고 해당 이미지를 상황분석서버(300)로 전송하여 분석 후 실시간 상황은 관리자(모바일 단말기 등)에게 자동으로 전달된다.The ascending microbubbles form a predetermined pattern when they operate normally on the transparent top plate 13, but the pattern is well observed in situations where they cannot operate normally (for example, situations where the floating filter medium aggregates with each other or does not move well). will not become The camera unit 150 monitors this pattern in real time and transmits the corresponding image to the situation analysis server 300. After analysis, the real-time situation is automatically transmitted to the manager (mobile terminal, etc.).

또한, 본 발명에 따른 상기 부상여과장치(120)는 바람직하게는 부상여과조(100) 내부 일측에 장착되며, 피처리수는 유입부(110)를 통해 부상여과조(100) 내부공간인 유입공간부(140)에 유입되고, 일측에 장착된 부상여과장치(120)를 경유하여 배출부(130)를 통해 배출된다.In addition, the flotation filter device 120 according to the present invention is preferably mounted on one side inside the flotation filter tank 100, and the water to be treated passes through the inlet part 110 to the inlet space, which is the inner space of the flotation filter tank 100. It flows into 140 and is discharged through the discharge unit 130 via the flotation filter 120 mounted on one side.

상기 부상여과장치(120)는 도 3에 도시한 바와 같이, 유입여과망(11) 및 배출여과망(12)이 장착된 여과탱크(10), 부상여재(20), 제1프로펠러(30), 제2프로펠러(40), 초음파발진기(50), 및 가이드격벽(60)을 포함한다.As shown in FIG. 3, the flotation filter device 120 includes a filter tank 10 equipped with an inlet filter net 11 and an outlet filter net 12, a flotation filter medium 20, a first propeller 30, a first 2 includes a propeller 40, an ultrasonic generator 50, and a guide bulkhead 60.

상기 본 발명의 바람직한 실시예로서 부상여과장치(120)는 여과탱크(10) 내부에 부상여재(20)가 수용되며, 상기 부상여재(20)는 피처리수와 함께 강제 대류 방식에 의해 여과탱크(10) 내부를 순환한다.As a preferred embodiment of the present invention, in the flotation filter device 120, the flotation filter medium 20 is accommodated inside the filter tank 10, and the flotation filter medium 20 is combined with the water to be treated in the filter tank by forced convection. (10) Circulate inside.

상기 본 발명에 따른 상기 여과탱크(10)는 피처리수가 아래에서 위 방향으로 내부로 유입되도록 저면에 유입여과망(11)이 장착된다. 상기 유입여과망(11)은 피처리수는 유입시키되, 내부의 부상여재(20)가 빠져나가지 못하게 막아주는 사이즈의 메쉬구조를 가질 것이 요구된다.In the filter tank 10 according to the present invention, an inflow filtering net 11 is mounted on the bottom so that the water to be treated flows into the inside from the bottom to the top. The inflow filter net 11 is required to have a mesh structure of a size that allows water to be treated to flow in and prevents the floating filter medium 20 from escaping.

또, 여과탱크(10) 내부에서 처리된 피처리수의 배출을 위해 상단 측벽에 상기 배출부(130)와 연결되는 배출여과망(12)이 장착된다. 상기 배출여과망(12)을 통해 처리수는 배출부(130)로 배출되지만, 부상여재(20)는 배출되지 않도록 하는 사이즈의 메쉬구조를 가질 것이 요구된다.In addition, a discharge filtering net 12 connected to the discharge unit 130 is mounted on the upper side wall of the filter tank 10 to discharge the treated water. Through the discharge filter net 12, the treated water is discharged to the discharge unit 130, but the flotation filter medium 20 is required to have a mesh structure of a size that prevents it from being discharged.

상기 제1프로펠러(30)는 여과탱크(10) 내부 일측(이하, 「제1측」이라 한다.) 상단에 장착된다.The first propeller 30 is mounted on an upper end of one side inside the filter tank 10 (hereinafter referred to as "first side").

상기 제1프로펠러(30)는 모터(미도시)에 의해 회전하면서 피처리수(부상여재(20)와 함께)를 수평방향으로 반대편인 타측(이하, 「제2측」이라 한다.)으로 흐름을 일으켜 이송시킨다.While rotating by a motor (not shown), the first propeller 30 flows the water to be treated (together with the floating filter media 20) to the other side opposite to the horizontal direction (hereinafter, referred to as the “second side”). raise and transport

제1프로펠러(30)에 의해 제2측으로 이송된 부상여재(20)를 포함하는 피처리수는 배출여과망(12)에 이르러 일부는 처리수로 배출되고, 부상여재(20)는 하방으로 중력 혹은 강제대류에 의해 침강한다.The water to be treated including the floating filter medium 20 transported to the second side by the first propeller 30 reaches the discharge filtration net 12, and some of it is discharged as treated water, and the floating filter medium 20 moves downward by gravity or Settled by forced convection.

상기 제2프로펠러(40)는 여과탱크(10)의 제2측 하단에 장착된다. 상기 제2프로펠러(40)는 모터(미도시)에 의해 구동되어 피처리수와 함께 침강된 부상여재(20)를 반대편인 제1측 방향으로 흐름을 일으켜 순환시킨다.The second propeller 40 is mounted on the lower end of the second side of the filter tank 10. The second propeller 40 is driven by a motor (not shown) to generate and circulate the flotation media 20 precipitated together with the water to be treated in the opposite direction to the first side.

상기 본 발명에서 초음파발진기(50)는 여과탱크(10)의 제1측 하단에 장착된다. 상기 초음파발진기(50)는 제2프로펠러(40)에 의해 이송된 피처리수와 부상여재(20)를 향하여 초음파를 방사한다. 상기 초음파의 방사는 부상여재(20)에 오염물질이 다량으로 부착되어 케이크를 형성할 경우 여과효율이 떨어지게 되므로 일정 주기, 예를 들어 역세 과정마다 수행될 수 있다. 이 과정에서 초음파 방사를 통해 탈리되는 케이크는 중력에 의해 하방으로 침강되어 부상여과조(100) 저부로부터 제거될 수 있다.In the present invention, the ultrasonic generator 50 is mounted at the bottom of the first side of the filter tank 10. The ultrasonic generator 50 radiates ultrasonic waves toward the water to be treated and the floating filter medium 20 transported by the second propeller 40 . The irradiation of the ultrasonic wave may be performed at a certain period, for example, every backwashing process, because the filtering efficiency decreases when a large amount of contaminants adhere to the flotation filter medium 20 to form a cake. In this process, the cake desorbed through ultrasonic radiation is sedimented downward by gravity and can be removed from the bottom of the flotation filter tank 100.

바람직하게는 상기 제1프로펠러(30), 제2프로펠러(40), 및 초음파발진기(50)는 부상여과조의 크기에 따라 복수개 일정간격으로 설치될 수 있으며, 측벽 내부 수용부(31, 41, 51)에 각각 별도 수납되어 보호되고, 그 입구는 여과망(32, 42, 52)에 의해 보호된다.Preferably, a plurality of the first propeller 30, the second propeller 40, and the ultrasonic generator 50 may be installed at regular intervals according to the size of the floating filter tank, and the side wall inner accommodating parts 31, 41, 51 ) are separately housed and protected, and the inlet is protected by filtering nets (32, 42, 52).

이와는 달리 상기 초음파 방사는 여과과정 중에도 지속적으로 수행하여도 되는데, 이는 하부로부터 유입되는 피처리수에 와류를 형성하여 오염물질의 부상여재(20)와의 접촉효율을 크게 개선할 수 있다. 이 경우 초음파에 의해 탈리되는 오염물질은 상대적으로 큰 물질인 경우 하방으로 침강되어 제거되거나 미세한 물질은 유입되는 원수와 함께 재부유되고 혼합되어 함께 처리되어진다. 이 과정에 의하면 부상여재(20)에 오염물질이 쉽게 부착되지 않아 오랜 기간 동안 별도의 세정 과정없이 처리하는 것이 가능하게 된다.Unlike this, the ultrasonic radiation may be continuously performed even during the filtration process, which can greatly improve the contact efficiency of contaminants with the floating filter medium 20 by forming a vortex in the water to be treated flowing from the bottom. In this case, contaminants desorbed by ultrasonic waves are removed by settling downward in the case of relatively large substances, or fine substances are resuspended together with the incoming raw water, mixed, and treated together. According to this process, contaminants are not easily attached to the flotation filter medium 20, making it possible to treat the flotation medium 20 without a separate cleaning process for a long period of time.

본 발명의 여과탱크(10) 내부에는 바람직하게는 제2측의 측벽에 일정 간격으로 이격되어 가이드격벽(60)이 수직방향으로 형성된다. 상기 가이드격벽(60)은 제1프로펠러(30)의 동작에 의해 제2측으로 이송되는 피처리수 및 부상여재(20)가 하방으로 이동하도록 가이드한다.Inside the filtration tank 10 of the present invention, preferably, guide partition walls 60 are formed in a vertical direction spaced apart from the sidewall of the second side at regular intervals. The guide bulkhead 60 guides the water to be treated and the floating filter medium 20 transported to the second side by the operation of the first propeller 30 to move downward.

상기 가이드격벽(60)은 제2측의 측벽과 적어도 1 이상의 지지대(61)에 의해 이격 지지되어질 수 있다.The guide bulkhead 60 may be spaced apart from the second side wall and supported by at least one supporter 61 .

바람직하게는 상기 가이드격벽(60)의 내부에 수직방향으로 적어도 1 이상의 산소공급부(62)가 장착되어진다. 상기 산소공급부(62)는 가이드격벽 내부에 장착된 산소공급관(62a)과 산소공급노즐(62b)로 구성된다. 상기 산소공급부(62)는 외부 산소공급실린더 내지 콤프레셔와 같은 산소공급장치(70)를 통해 산소를 공급받는다.Preferably, at least one oxygen supply unit 62 is mounted in the vertical direction inside the guide partition wall 60. The oxygen supply unit 62 is composed of an oxygen supply pipe 62a and an oxygen supply nozzle 62b mounted inside the guide partition wall. The oxygen supply unit 62 receives oxygen through an external oxygen supply cylinder or an oxygen supply device 70 such as a compressor.

따라서, 여과탱크(10) 내에서 피처리수와 함께 부상하는 과정에서 오염물질이 흡착되고, 가이드격벽(60)에 의해 하방으로 가이드되는 과정에서 상기 산소공급부(62)에서 공급되는 산소 미세기포에 의해 흡착된 유기물질 등의 오염물질을 산화시켜 처리할 수 있어 폐수의 처리효율은 추가적으로 개선되어진다.Therefore, contaminants are adsorbed in the process of floating together with the water to be treated in the filtration tank 10, and in the process of being guided downward by the guide partition wall 60, the oxygen microbubbles supplied from the oxygen supplier 62 It is possible to oxidize and treat contaminants such as organic matter adsorbed by the wastewater treatment efficiency.

상기와 같은 본 발명의 구성에 의하면 부상여재(20)가 내부에서 순환하는 방식을 채용하여 기존 부상여과 방식에 비해 많은 양을 수용할 수 있게 되어 처리효율은 크게 개선되어질 수 있다.According to the configuration of the present invention as described above, by adopting a method in which the flotation filter medium 20 circulates inside, it is possible to accommodate a larger amount than the conventional flotation filtration method, and thus the treatment efficiency can be greatly improved.

상기 제1프로펠러(30) 및 제2프로펠러(40)의 크기 및 최적의 회전속도는 피처리수의 점도, 양, 내지 수용된 부상여재의 함량 등에 따라 달리 설정되어질 수 있음은 물론이다.Of course, the size and optimum rotational speed of the first propeller 30 and the second propeller 40 may be set differently depending on the viscosity and amount of the water to be treated or the content of the flotation media contained therein.

상기와 같이, 본 발명의 바람직한 실시 예를 참조하여 설명하였지만 해당 기술 분야의 숙련된 당업자라면 하기의 특허청구범위에 기재된 본 발명의 사상 및 영역으로부터 벗어나지 않는 범위 내에서 본 발명을 다양하게 수정 및 변경시킬 수 있음을 이해할 수 있을 것이다. As described above, although it has been described with reference to the preferred embodiments of the present invention, those skilled in the art will variously modify and change the present invention within the scope not departing from the spirit and scope of the present invention described in the claims below. You will understand that it can be done.

10: 여과탱크
20: 부상여재
30: 제1프로펠러
40: 제2프로펠러
50: 초음파발진기
60: 가이드격벽
100: 부상여과조
110: 유입부
120: 부상여과장치
130: 배출부
150: 카메라부
200: 고온살균부
300: 상황분석서버
10: filter tank
20: wound media
30: first propeller
40: second propeller
50: ultrasonic oscillator
60: guide bulkhead
100: flotation filter
110: inlet
120: flotation filter
130: discharge unit
150: camera unit
200: high temperature sterilization unit
300: situation analysis server

Claims (4)

유량조정조; 유량조정조로부터 유입되는 피처리수 중의 인을 제거하는 혐기조; 상기 혐기조로부터 유입되는 피처리수 중의 질산성 질소를 제거하는 무산소조; 상기 무산소조로부터 유입되는 피처리수 중으로 공기를 폭기시켜 질소를 질산화시키는 호기조; 상기 호기조로부터 유입되는 피처리수를 상등액과 슬러지로 분리시키는 침전조; 열교환에 의해 피처리수를 고온살균처리하는 고온살균부; 및 부상여과조를 포함하되,
상기 고온살균부는 부상여과조 전단에 설치되며, 피처리수가 이송되는 내관, 및 상기 내관을 둘러싸고 내부에 고온의 열매체가 흘러 상기 내관의 피처리수에 고온의 열을 공급하는 외관으로 이루어지고,
상기 부상여과조는 피처리수가 유입되는 유입부, 피처리수 유입공간에 장착되는 부상여과장치, 및 피처리수가 배출되는 배출부를 포함하되,
상기 부상여과장치는,
저면에 장착된 유입여과망 및 상단 일측에 장착된 배출여과망을 갖고 내부에 부상여재를 수용하여 피처리수를 여과처리하는 여과탱크; 상기 여과탱크내 수용되며 피처리수와 함께 부상하면서 오염물질을 제거하는 부상여재; 여과탱크내 상부 제1측에 장착되어, 반대편인 제2측으로 피처리수를 이동시키는 제1프로펠러; 여과탱크내 하부 제2측에 장착되어, 반대편인 제1측으로 피처리수를 이동시키는 제2프로펠러; 여과탱크내 하부 제1측에 장착되어 상기 제2프로펠러에 의해 이동된 피처리수와 함께 이동되는 부상여재에 초음파를 방사하는 초음파발진기; 및 여과탱크내 제2측 벽면과 이격되어 형성되어, 피처리수와 부상여재를 하방으로 순환시키도록 가이드하는 가이드격벽을 포함하는 것을 특징으로 하는 처리효율이 개선된 부상여과조를 포함하는 하수고도처리장치.
flow control tank; an anaerobic tank for removing phosphorus in the water to be treated flowing in from the flow control tank; An anoxic tank for removing nitrate nitrogen from the water to be treated flowing from the anaerobic tank; an aerobic tank for nitrifying nitrogen by aerating air into the water to be treated flowing from the anoxic tank; a sedimentation tank which separates the water to be treated from the aerobic tank into supernatant and sludge; a high-temperature sterilization unit for high-temperature sterilization of water to be treated by heat exchange; And including a floating filter tank,
The high-temperature sterilization unit is installed at the front end of the flotation filtration tank, and includes an inner tube through which the water to be treated is transported, and an exterior that surrounds the inner tube and supplies high-temperature heat to the water to be treated in the inner tube by flowing a high-temperature heat medium inside,
The flotation filter tank includes an inlet through which the water to be treated flows, a flotation filter installed in the inflow space of the water to be treated, and an outlet through which the water to be treated is discharged,
The floating filter device,
A filter tank having an inlet filter net attached to the bottom and a discharge filter net attached to one side of the top, and accommodating the flotation filter medium therein to filter the water to be treated; a flotation filter medium accommodated in the filtration tank and removing contaminants while floating together with the water to be treated; A first propeller mounted on a first side of the upper part of the filter tank to move the water to be treated to a second side opposite to the first side; a second propeller mounted on a lower second side of the filtration tank to move the water to be treated to the opposite first side; an ultrasonic generator mounted on a lower first side of the filter tank and radiating ultrasonic waves to the floating filter media moving together with the water to be treated moved by the second propeller; and a guide bulkhead formed to be spaced apart from the second side wall of the filtration tank and guiding the water to be treated and the flotation media to circulate downward. Device.
삭제delete 제 1항에 있어서,
상기 제1프로펠러, 제2프로펠러, 및 초음파발진기는 측벽 내부 수용부에 수납되어지는 것을 특징으로 하는 실시간 모니터링이 가능한 부상여과조를 포함하는 하수고도처리장치.
According to claim 1,
The first propeller, the second propeller, and the ultrasonic generator are housed in the inner accommodating part of the side wall.
제 1항에 있어서,
가이드격벽의 내부에 수직방향으로 적어도 1 이상의 산소공급부가 장착되며, 상기 산소공급부는 산소공급관과 산소공급노즐로 구성되어 하강하는 부상여재와 피처리수에 함유된 오염물질을 제거하는 것을 특징으로 하는 하수고도처리장치.
According to claim 1,
At least one oxygen supply unit is mounted in the vertical direction inside the guide bulkhead, and the oxygen supply unit is composed of an oxygen supply pipe and an oxygen supply nozzle, and removes contaminants contained in the floating filter medium and the water to be treated. Sewage advanced treatment system.
KR1020210113540A 2021-08-26 2021-08-26 Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency KR102497137B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020210113540A KR102497137B1 (en) 2021-08-26 2021-08-26 Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020210113540A KR102497137B1 (en) 2021-08-26 2021-08-26 Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency

Publications (1)

Publication Number Publication Date
KR102497137B1 true KR102497137B1 (en) 2023-02-08

Family

ID=85225818

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020210113540A KR102497137B1 (en) 2021-08-26 2021-08-26 Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency

Country Status (1)

Country Link
KR (1) KR102497137B1 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61103592A (en) * 1984-10-27 1986-05-22 Toshiba Corp Manufacturing apparatus of demineralized water
KR100971287B1 (en) * 2009-08-28 2010-07-20 주식회사 라인테크 Sterilizer for medical waste water
KR100986036B1 (en) * 2010-08-17 2010-10-07 (주)도드람환경연구소 Method for treating livestock excretions

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61103592A (en) * 1984-10-27 1986-05-22 Toshiba Corp Manufacturing apparatus of demineralized water
KR100971287B1 (en) * 2009-08-28 2010-07-20 주식회사 라인테크 Sterilizer for medical waste water
KR100986036B1 (en) * 2010-08-17 2010-10-07 (주)도드람환경연구소 Method for treating livestock excretions

Similar Documents

Publication Publication Date Title
EP2254842B1 (en) Method and device for the treatment of waste water
US6413427B2 (en) Nitrogen reduction wastewater treatment system
CN101618925B (en) Sewage treatment device
CN105481177A (en) Low-consumption nitrification and denitrification coal chemical wastewater advanced treatment device
CN103112991B (en) Coking wastewater treatment system and coking wastewater treatment method
CN109704516B (en) Treatment system and treatment method for aniline wastewater
KR100856442B1 (en) Plug flow bioreactor with micro bubble for treatment of wastewater
CN102774998A (en) High-salinity high-chromaticity printing and dyeing wastewater recovery process and equipment thereof
KR102581817B1 (en) Advanced wastewater treatment apparatus comprising floating filter tank capable of monitoring
JP4409532B2 (en) Apparatus for treating wastewater containing high-concentration nitrogen such as livestock wastewater and manure, and its treatment method
KR101541070B1 (en) method and device for controlling using turbulence stimulation and filter member
KR102496233B1 (en) Advanced wastewater treatment apparatus comprising complex filter type
KR102452662B1 (en) Wastewater treatment apparatus having the circulation guide unit of penton oxidation and treated water
AU2006300978B2 (en) SAF system and method involving specific treatments at respective stages
CN207512026U (en) For the advanced treatment apparatus being for further processing to biochemical treatment tail water
KR102497137B1 (en) Advanced wastewater treatment apparatus comprising floating filter tank with improved treating efficiency
KR100610589B1 (en) Effluent treatment system for aquafarm
JP2006289153A (en) Method of cleaning sewage and apparatus thereof
KR101989883B1 (en) Purification plant for livestock waste water
KR101817471B1 (en) Wastewater Treatment System
KR102452659B1 (en) Wastewater treatment apparatus having the circulation guide part of the treated water
KR102452663B1 (en) Wastewater treatment apparatus which is controllable the inflow of the treated water and penton oxidation
KR102452661B1 (en) Wastewater treatment apparatus which is controllable the inflow of the treated water
KR102581775B1 (en) Advanced wastewater treatment apparatus comprising floating filter tank
KR102497135B1 (en) Advanced wastewater complex treatment apparatus with three step filtering type

Legal Events

Date Code Title Description
E701 Decision to grant or registration of patent right
GRNT Written decision to grant