KR20040001286A - A way and a device to purify sevage and waste water by using a bed biofilm - Google Patents

A way and a device to purify sevage and waste water by using a bed biofilm Download PDF

Info

Publication number
KR20040001286A
KR20040001286A KR1020020036429A KR20020036429A KR20040001286A KR 20040001286 A KR20040001286 A KR 20040001286A KR 1020020036429 A KR1020020036429 A KR 1020020036429A KR 20020036429 A KR20020036429 A KR 20020036429A KR 20040001286 A KR20040001286 A KR 20040001286A
Authority
KR
South Korea
Prior art keywords
biofilm
wastewater
carrier
reaction tank
fixed
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
KR1020020036429A
Other languages
Korean (ko)
Inventor
박경북
윤여진
손석희
명규남
이동훈
Original Assignee
(주)이앤엠코리아
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)이앤엠코리아 filed Critical (주)이앤엠코리아
Priority to KR1020020036429A priority Critical patent/KR20040001286A/en
Publication of KR20040001286A publication Critical patent/KR20040001286A/en
Ceased legal-status Critical Current

Links

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
    • C02F3/06Aerobic processes using submerged filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/08Aerobic processes using moving contact bodies
    • 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
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • C02F3/1273Submerged membrane bioreactors
    • 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
    • C02F3/1278Provisions for mixing or aeration of the mixed liquor
    • 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
    • C02F3/20Activated sludge processes using diffusers
    • 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
    • C02F2003/001Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
    • 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)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE: Provided is an advanced sewage and wastewater treatment apparatus having both of fixed biomedia and fluidized biomedia in a reactor to increase treatment efficiency and reduce cost. CONSTITUTION: The apparatus comprises a reactor(10) with a diffuser(20) and operating under aerobic condition, biomedia(30) fixed in the reactor(10) to be a fixed biofilm, and granular biomedia(40) arranged between the fixed biomedia(30) and fluidized in the reactor(10) by air diffused by the diffuser(20).

Description

생물막을 이용한 오ㆍ폐수의 고도처리방법 및 장치{A way and a device to purify sevage and waste water by using a bed biofilm}Advanced method and apparatus for treating wastewater using biofilms {A way and a device to purify sevage and waste water by using a bed biofilm}

본 발명은 고정상 생물막과 유동상 생물막을 이용한 오ㆍ폐수처리방법 및 장치에 관한 것으로, 보다 구체적으로는 하나의 반응조 내부에 고정상 담체와 유동상담체를 동시에 침지시켜 고정상 생물막과 유동상 생물막의 장점을 결합시키고 단점을 보완할 수 있는 시스템으로 구성하여 유기물, 질소, 인의 높은 제거효율을 얻을 수 있도록 한 고도처리방식이다.The present invention relates to a method and apparatus for treating sewage and wastewater using a fixed bed biofilm and a fluidized bed biofilm, and more specifically, by simultaneously immersing a fixed bed carrier and a fluid carrier in one reactor, It is a high-level treatment method that can combine the system and make up for the shortcomings and get high removal efficiency of organic matter, nitrogen and phosphorus.

통상 생물막(담체)을 이용한 오ㆍ폐수처리방법은 고정상 생물막을 이용하여 처리하는 방법과 유동상 생물막을 이용하여 처리하는 방법이 있는 것으로, 고정상 생물막을 이용한 종래의 처리방법으로서는 생물막이 형성되는 여과상을 고정시킨 상부로 회전분무기를 이용하여 처리수를 살수시킴으로서 처리하는 살수여상법과, 처리수의 표면에 생물막이 형성되는 회전원판을 반쯤 침지시켜 처리하는 회전원판법(RBC; Rotating Biological Contactor)과, 생물막이 형성되는 여과막을 처리수에 침지시켜 생물막에 의한 생물학적 처리와 여과에 의한 물리적 처리가 가능토록 한 생물막여과법(SBF; Super-clean Biological Filters)이 있고, 입자 형태의 담체를 충진시킨 여과상의 하부로 공기를 분사시켜 처리효율을 높인 고정상 BAF(Biological Aerated Filters) 등이 있다.In general, the wastewater treatment method using a biofilm (carrier) includes a treatment method using a fixed bed biofilm and a method using a fluid bed biofilm. As a conventional treatment method using a fixed bed biofilm, a filter bed on which a biofilm is formed is used. Spraying water treatment method to treat the treatment water by spraying the treated water using a rotating sprayer to the upper portion fixed to the rotating disk method (RBC; Rotating Biological Contactor) to immerse half the immersion of the rotating disk is formed biofilm on the surface of the treated water, Super-clean Biological Filters (SBF), in which the filtration membrane in which the biofilm is formed is immersed in the treated water to enable biological treatment by the biofilm and physical treatment by filtration. And fixed-phase Biological Aerated Filters (BAF), which are used to inject air into the air to increase processing efficiency.

즉, 생물막 형성 위한 담체가 여과상의 형태로 일정한 위치에 고정시켜 처리하는 것으로, 담체의 일부구간에 부착된 생물막은 호기성 조건 상태에서 증식되고 또 다른 일부구간에 부착된 생물막은 무산소 조건 내지 혐기성 조건 상태에서 증식되어 질소와 인이 제거될 수 있는 다양한 생물종의 서식 환경이 제공됨으로서 다양한 생물종의 확보로 체류시간이 긴 미생물이 존재하기 때문에 충격부하에 강하다는 점과, 부유물질(SS; Suspended Solid) 및 슬러지의 부착이 용이하여 침전조가 필요 없게 됨으로서 부지면적을 절감시킬 수 있어 유지 및 설치비용이 저렴하다는 장점이 있는 반면, 담체에 생물막이 형성될 때까지의 소요시간이 길고, 유기물의 농도가 낮을 경우 생물막의 탈리가 진행되어 탈리된 생물막의 원상회복이 어렵고, 생물막의 과다번식 및 걸러진 부유물질(SS)에 의하여 담체 내의 부분적인 폐색 현상이 발생되는 처리효율을 저하시킬 수 있는 요인이 있는 단점이 있는 것이다.That is, the carrier for forming the biofilm is fixed and treated at a predetermined position in the form of a filter phase, wherein the biofilm attached to a part of the carrier is grown in aerobic conditions and the biofilm attached to another part is anoxic to anaerobic. It provides a habitat for a variety of species that can be removed from nitrogen and phosphorus by proliferating in the presence of microorganisms. ), And it is easy to attach the sludge, which eliminates the need for the settling tank, which can reduce the area of land, and thus the maintenance and installation costs are low. On the other hand, the time required for the formation of the biofilm on the carrier is long, and the concentration of organic matter is high. If it is low, biofilm desorption proceeds and it is difficult to recover the detached biofilm. Due to the suspended suspended solids (SS) is a disadvantage that there is a factor that can reduce the treatment efficiency in which a partial blockage phenomenon occurs in the carrier.

한편, 유동상 생물막을 이용한 처리방법은 입자 형태의 담체를 반응조에 침지시키고 공기로 밀어올리거나 수류를 조정하여 담체가 떠 있는 상태에서 생물막과 처리수를 접촉시켜 고도처리하는 공법으로, 고정상과는 달리 담체에 부유물질 및 슬러지의 부착이 어려워 순수한 질산화 박테리아의 부착 및 성장이 상대적으로 우수해 암모니아, 아질산의 제거능력이 짧은 시간 내에도 매우 탁월하다는 점과, 담체가 유동되면서 서로 충돌되기 때문에 담체의 생물막의 두께가 일정하게 유지됨으로서 생물막의 과다 증식을 억제할 수 있다는 점과, 진 비중이 일반적인 슬러지 비중 보다 높아 활성슬러지와 함께 유동하면서 공기와의 충돌에 의하여 공기를 잘게 부수기 때문에 용존 산소율을 상승시킬 수 있어 처리효율을 높일 수 있는 요소가 충분한 장점이 있는 반면, 부유물질 및 슬러지를 제거하기 위한 별도의 처리조가 필요하고, 담체가 유동되어 외부로 유출되는 문제점이 있어 담체를 일정량씩 주기적으로 공급하거나 담체의 유출을 방지하기 위한 별도의 장치를 설치하여야 하기 때문에 고정식에 비하여 부지면적과, 설치 및 유지비용이 상승되어 경제적 부담이 있는 단점이 있다.On the other hand, the treatment method using a fluidized bed biofilm is a method of immersing the carrier in the form of particles in the reaction tank and pushing it up into the air or adjusting the water flow to contact the biofilm and the treated water in a state where the carrier is floating, which is highly processed. In contrast, it is difficult to attach suspended solids and sludge to the carrier, so that the adhesion and growth of pure nitrifying bacteria is relatively excellent, so that the ability to remove ammonia and nitrite is excellent even within a short time. By keeping the thickness of the biofilm constant, it is possible to suppress the overgrowth of the biofilm, and since the specific gravity is higher than the general sludge specific gravity, it flows with activated sludge and crushes the air by collision with air, thereby increasing the dissolved oxygen rate. There is an advantage that there are enough elements to increase the processing efficiency. On the other hand, there is a need for a separate treatment tank to remove suspended solids and sludge, there is a problem that the carrier is flowed out to the outside to supply the carrier periodically by a certain amount or to install a separate device to prevent the outflow of the carrier Due to the increase in the land area, installation and maintenance costs compared to the fixed type has the disadvantage that there is an economic burden.

따라서 본 발명은 상기한 종래의 문제점을 해결하기 위하여 안출한 것으로서, 본 발명의 목적은 생물막을 이용하여 오ㆍ폐수를 처리할 경우 고정상 생물막과 유동상 생물막의 단점을 각각의 장점으로 상호 보완하고 장점을 부가시켜 경제적 부담은 절감하면서 처리효율은 극대화시킬 수 있도록 하고자 함이다.Therefore, the present invention has been made to solve the above-mentioned conventional problems, an object of the present invention is to complement the disadvantages of the fixed bed biofilm and fluidized bed biofilm with their respective advantages and advantages when treating the waste water using a biofilm In order to reduce the economic burden and maximize the processing efficiency.

이를 위하여 하나의 반응조에 일정 간격으로 여과상의 고정매체(담체)를 설치하여 고정상 생물막을 형성시키고, 여과상의 고정매체(담체) 사이에 입자상의 유동매체(담체)를 형성시켜 하부로부터 분사되는 공기방울 입자에 의하여 부유되는 유동상 생물막을 형성시켜, 고정상 생물막에 의한 부유물질 및 슬러지의 여과기능이 있도록 하고, 유동상 생물막에 의한 충돌 현상으로 고정상 생물막의 과다증식억제 및 용존산소량을 증가시키고, 고정상 생물막에 의한 유동상 생물막의 유출을 방지시킨 것이다.To this end, fixed fixed media (carriers) are installed in one reactor at a predetermined interval to form a fixed biofilm, and a particulate fluid medium (carriers) is formed between the fixed fixed media (carriers) and air bubbles sprayed from the bottom. It forms a fluidized biofilm suspended by the particles, so that the suspended solids and sludge filtration function by the fixed bed biofilm, the collision phenomenon by the fluidized bed biofilm increases the suppression of overgrowth and dissolved oxygen of the fixed bed biofilm, fixed bed biofilm It is to prevent the outflow of fluidized bed biofilm by.

도 1은 본 발명의 일 실시예에 따른 구성을 나타낸 일부 절개 사시도.1 is a partial cutaway perspective view showing a configuration according to an embodiment of the present invention.

도 2는 도 1의 단면도.2 is a cross-sectional view of FIG.

도 3은 본 발명의 또 다른 실시에를 나타낸 일부 절개 사시도.3 is a partially cutaway perspective view of yet another embodiment of the present invention.

도 4는 도 3의 단면도.4 is a cross-sectional view of FIG.

도 5는 본 발명의 제 3 실시예를 나타낸 일부 절개 사시도.5 is a partially cutaway perspective view showing a third embodiment of the present invention.

도 6은 도 5의 단면도.6 is a cross-sectional view of FIG.

<도면의주요부분에대한부호의설명>Explanation of symbols on the main parts of the drawing

10: 반응조 20: 산기장치10: reactor 20: diffuser

30, 30a: 여과상 담체 40: 입자상 담체30, 30a: filter bed carrier 40: particulate carrier

50: 스크린 60: 부체50: screen 60: floating body

본 발명은 생물막을 이용한 오ㆍ폐수처리방법에 있어서, 하나의 반응조에 고정상 생물막과 유동상 생물막이 동시에 형성되어진 처리장치를 이용하여 오ㆍ폐수를 처리하는 방법이다.The present invention relates to a wastewater treatment method using a biofilm, wherein the wastewater is treated using a treatment apparatus in which a fixed bed biofilm and a fluidized bed biofilm are simultaneously formed in one reactor.

이하, 첨부 도면을 참조하여 본 발명을 실시하기 위한 처리장치의 구성 및 작용을 보다 상세하게 설명하기로 한다.Hereinafter, with reference to the accompanying drawings will be described in more detail the configuration and operation of the processing apparatus for carrying out the present invention.

도 1과 도 2에 도시된 바와 같이, 본 발명은 산기장치(20)가 구비되어 호기성 상태로 운전되는 반응조(10) 내부에 여과상 담체(30)가 고정된 상태로 나열되어 고정상 생물막을 형성토록 하고, 나열된 여과상 담체(30) 사이에 입자상 담체(40)가 형성되어 상기 산기장치(20)로부터 분사되는 공기 입자에 의하여 유동상 생물막을 형성토록 한 것이다.As shown in FIG. 1 and FIG. 2, the present invention is provided with an acidic device 20 and is arranged in a state in which the filtration carrier 30 is fixed inside the reaction tank 10 operated in an aerobic state to form a stationary biofilm. The particulate carrier 40 is formed between the listed filtration carriers 30 so that the fluidized biofilm is formed by the air particles sprayed from the air diffuser 20.

이때 상기 여과상 담체(30)는 반응조(10)의 중심부에 침수된 상태로 떠 있도록 고정시킴으로서 여과상 담체(30)의 상, 하부로 입자상 담체(40)의 유동이 가능토록 설치하는 것으로, 반응조(10)의 후방에는 입자상 담체(40)의 유출을 방지하기 위한 스크린(50)이 설치되는 것이고, 반응조(10)의 중심부에는 처리수의 정체를 방지하기 위한 교반장치(60)가 설치되는 것이다.At this time, the filter bed carrier 30 is installed to allow the flow of the particulate carrier 40 to the upper and lower portions of the filter bed carrier 30 by fixing the floating bed in the submerged state in the center of the reaction tank 10. The rear of the (10) is provided with a screen 50 for preventing the outflow of the particulate carrier 40, the central portion of the reaction tank 10 is provided with a stirring device 60 for preventing the stagnation of the treated water. .

이때 상기 여과상 담체(30) 중 반응조(10)의 유입부에 설치되는 최초 여과상 담체(30a)를 가장 큰 형태로 하고 후방으로 점차 작아지는 형태의 여과상 담체(30b)(30c).. (30n)를 형성토록 함으로서 반응조(10) 전단에 침전조를 거치지 않고도 부유물질을 동시에 처리할 수 있도록 할 수 있는 것이다.At this time, the first filter bed carrier (30a) installed in the inlet of the reaction tank (10) of the filter bed carrier 30 to the largest form and gradually decreases toward the rear of the filter bed carrier (30b) (30c). By forming (30n) it is possible to simultaneously handle the suspended matter without passing through the settling tank in the front of the reaction tank (10).

이때 반응조(10)의 유출부에 설치되는 최후의 여과상 담체(30n)를 도 3과 도 4에 도시된 바와 같이 반응조(10)의 상단부와 하단부까지 걸쳐지도록 설치할 경우, 입자상 담체(40)의 유출을 방지하기 위하여 설치되는 스크린(50)의 역할을 동시에 수행할 수 있어 스크린(50)의 별도 설치가 필요치 않는 것이다.At this time, when the last filter bed carrier (30n) installed in the outlet of the reaction tank 10 to cover the upper end and the lower end of the reaction tank 10, as shown in Figure 3 and 4, the particulate carrier 40 In order to prevent leakage, the screen 50 may be installed at the same time, so the separate installation of the screen 50 is not necessary.

또한 상기 반응조(10)의 바닥은 일측으로 경사면(11)을 두어 경사면(11)으로 상기 산기장치(20)가 구비토록 함으로서 입자상 담체(40)가 가라앉을 경우에도 경사면(11)에 구비된 산기장치(20)에 의해 유동이 용이하도록 되어 있다.In addition, the bottom of the reaction tank 10 has an inclined surface 11 on one side, so that the diffuser device 20 is provided on the inclined surface 11, even when the particulate carrier 40 sinks. The device 20 facilitates the flow.

한편, 도 5와 도 6은 본 발명의 또 다른 실시예를 도시한 것으로, 상기 여과상 담체(30)를 부체(60) 등에 매달아 반응조(10)에 반부유식으로 설치하여 반부유식 생물막을 추가로 형성시킬 수 있는 것이다.On the other hand, Figure 5 and Figure 6 shows another embodiment of the present invention, the filter bed carrier 30 is suspended in the floating body 60, etc. installed in the semi-floating system in the reaction tank 10 to further add a semi-floating biofilm. It can be formed.

이는 회전원판법(RBC; Rotating Biological Contactor)의 원리를 이용한 것으로 별도의 동력원 없이 수중의 유동과 폭기 시 발생되는 상하좌우의 유체 흐름에 따라 여과상 담체(30)가 편심을 받아 회전이 가능하기 때문에 호기성 미생물 뿐 아니라 내부의 혐기성 미생물이 살 수 있는 다양한 환경이 조성되어 다양한 미생물의 서식공간을 제공할 수 있는 것이고, 반응조(10)의 부하변동에 강하고 고정상 생물막의 대량 탈리 시 타 반응조의 부유상을 투입함으로서 미생물의 농도를 유지할 수 있는 특징이 있는 것이다.This is based on the principle of Rotating Biological Contact (RBC), and because the filtration carrier 30 is eccentric and rotates according to the fluid flow in the water and aeration caused by underwater flow and aeration without a separate power source. In addition to aerobic microorganisms as well as various anaerobic microorganisms inside the environment can be created to provide a habitat for a variety of microorganisms, it is resistant to the load fluctuations of the reaction tank (10) and when a large amount of desorption of the fixed-phase biofilm, There is a feature that can maintain the concentration of microorganisms by adding.

또한, 본 발명은 연속흐름식 또는 회분식반응조에 모두 적용할 수 있는 것이고, 처리수의 유입 및 유출 방향을 다양하게 변경시켜도 가능한 것이다.In addition, the present invention can be applied to both a continuous flow or a batch reaction tank, it is possible to vary the inflow and outflow direction of the treated water.

따라서 상기와 같이 구성된 본 발명의 처리장치는 하나의 반응조(10) 내부에 여과상 담체(30)에 의한 고정상 생물막과 입자상 담체(40)에 의한 유동상 생물막이 동시에 형성될 수 있는 것으로, 이 장치를 이용하여 오ㆍ폐수를 처리하면, 입자상 담체(40)가 여과상 담체(30) 사이에 형성되어 입자상 담체(40)의 상하좌우로 유동토록 됨으로서 유동상 생물막 끼리의 충돌과 더불어 고정상 생물막에도 충돌되어 유동상 생물막의 MLSS 농도를 일정하게 유지할 수 있을 뿐 아니라, 고정상 생물막의 과잉증식을 억제시킬 수 있어 외부의 막힘 현상을 지연, 방지할 수 있고, 고정상 생물막에 의한 유동상 생물막의 유출을 방지할 수 있어 각각의 단점을 상호보완할 수 있는 것이다.Therefore, the treatment apparatus of the present invention configured as described above is capable of simultaneously forming a fixed bed biofilm by the filter carrier 30 and a fluid bed biofilm by the particulate carrier 40 in one reactor 10. When the wastewater is treated by using, the particulate carrier 40 is formed between the filter carriers 30 so as to flow up, down, left, and right of the particulate carrier 40, so that the fluidized biofilms collide with each other and collide with the fixed bed biofilm. Not only can the MLSS concentration of the fluidized bed biofilm be kept constant, but also the overgrowth of the fixed bed biofilm can be suppressed, which can delay and prevent external clogging, and prevent the fluidized bed biofilm from flowing out by the fixed bed biofilm. It can be used to complement each disadvantage.

또한, 고정상 생물막에 의한 부유물질 및 슬러지의 여과가 가능하여 이를 처리하기 위한 침전조 등 별도의 처리장치가 필요치 않은 고정상 생물막의 장점과,생물막의 형성 시간이 짧고, 산기장치(20)로부터 분사되는 공기입자와의 충돌현상으로 공기입자를 잘게 부수어 산소 전달효율을 크게 할 수 있기 때문에 처리시간이 짧은 유동상 생물막의 장점이 결합됨으로서 배가의 장점을 얻을 수 있는 것이다.In addition, it is possible to filter the suspended solids and sludge by the fixed bed biofilm, the advantage of the fixed bed biofilm that does not require a separate treatment device, such as a sedimentation tank for processing it, the formation time of the biofilm is short, the air injected from the air diffuser 20 Since the collision with the particles can break up the air particles to increase the oxygen transfer efficiency, the advantages of the fluidized biofilm with short processing time can be combined to obtain the advantages of doubled.

상술한 바와 같이 본 발명은 한 반응조 내에서 서로 다른 장, 단점이 있는 두 가지 생물막을 동시에 사용하여 각각의 단점은 상호보완되어 해결할 수 있고, 각각의 장점은 배가시켜 경제적 부담은 절감하면서 처리효율은 극대화시킬 수 있는 생물막을 이용한 오ㆍ폐수처리가 가능하게 되는 것이다.As described above, the present invention can be solved by complementing each of the disadvantages by simultaneously using two different biofilms having different advantages and disadvantages in one reactor, and each advantage is doubled to reduce the economic burden while reducing the treatment efficiency. Wastewater treatment using biofilms that can be maximized is enabled.

따라서 미생물 종의 다양성을 확보하여 수리적, 유기물, 독성물질의 충격에 강하고, 적은 잉여 슬러지 발생으로 침전조의 용량이 작아지고, 장치의 구조가 간단해서 유지관리가 용이하며, 슬러지의 반송이 불필요하고, 두가지 생물막의 구성으로 호기성 조건에서도 탈질 반응이 가능하며, 유동성 담체의 충돌에 의해 생물막의 탈리와 부착이 쉬워져 생물막의 MLSS 농도를 일정하게 유지할 수 있어 정상상태에서 반응조의 운전이 용이하고 안정적 수질확보가 가능한 것이다.Therefore, it secures the diversity of microbial species, so it is strong against the impact of hydraulics, organics and toxic substances, and the capacity of sedimentation tank is small due to the generation of small excess sludge, the structure of the device is simple, maintenance is easy, and sludge transportation is unnecessary. The composition of two biofilms enables denitrification under aerobic conditions, and the detachment and attachment of biofilms is easy due to the collision of fluid carriers, so that the MLSS concentration of the biofilms can be kept constant. Would be possible.

Claims (7)

생물막을 이용한 오ㆍ폐수처리방법에 있어서, 호기성 상태로 운전되는 하나의 반응조에 내부에 고정상 생물막과 유동상 생물막을 동시에 형성시켜 오ㆍ폐수를 처리하는 생물막을 이용한 오ㆍ폐수의 고도처리방법.A wastewater treatment method using a biofilm, comprising: a fixed biofilm and a fluidized biofilm formed inside a single reaction tank operated in an aerobic state to treat wastewater and wastewater. 제 1항에 있어서, 고정상 생물막과 유동상 생물막이 형성된 반응조에 반부유식 생물막을 추가 형성시켜 오ㆍ폐수를 처리하는 생물막을 이용한 오ㆍ폐수의고도처리방법.The advanced treatment method for wastewater and wastewater using a biofilm according to claim 1, wherein a semi-floating biofilm is further formed in a reaction tank in which the fixed bed biofilm and the fluidized bed biofilm are formed. 산기장치(20)가 구비되어 호기성 상태로 운전되는 반응조(10) 내부에 여과상 담체(30)가 고정된 상태로 나열되어 고정상 생물막을 형성토록 하고, 나열된 여과상 담체(30) 사이에 입자상 담체(40)가 형성되어 상기 산기장치(20)로부터 분사되는 공기 입자에 의하여 유동상 생물막을 형성토록 함을 특징으로 하는 생물막을 이용한 오ㆍ폐수의 고도처리장치.The filter device carrier 30 is arranged in a fixed state inside the reaction tank 10 which is provided with an acidic device 20 to operate in an aerobic state to form a fixed bed biofilm, and the particulate carrier between the listed filter carriers 30. (40) is formed to form a fluidized biofilm by the air particles injected from the air diffuser (20), the advanced treatment device for wastewater and wastewater using a biofilm. 제 3항에 있어서, 상기 여과상 담체(30) 중의 일부를 부체에 고정시켜 반부유식으로 형성토록 함을 특징으로 하는 생물막을 이용한 오ㆍ폐수의 고도처리장치.4. An advanced treatment apparatus for wastewater and wastewater using a biofilm according to claim 3, wherein a part of said filtration carrier (30) is fixed to a floating body to form a semi-floating system. 제 3항 또는 제 4항에 있어서, 상기 반응조(10)의 유입부에 설치되는 최초여과상 담체(30a)를 가장 큰 형태로 하고 후방으로 점차 작아지는 형태로 형성시킴을 특징으로 하는 생물막을 이용한 오ㆍ폐수의 고도처리장치.The method of claim 3 or 4, wherein the first filtration carrier (30a) installed in the inlet of the reaction tank 10 is formed in the form of the largest and gradually decreases to the rear form using a biofilm Advanced Wastewater Treatment System. 제 3항 또는 제 4항에 있어서, 상기 반응조(10)의 유출부에 설치되는 최후의 여과상 담체(30n)를 반응조(10)의 상단부와 하단부까지 걸쳐지도록 형성시킴을 특징으로 하는 생물막을 이용한 오ㆍ폐수의 고도처리장치.The method of claim 3 or 4, wherein the last filter bed carrier 30n provided in the outlet of the reaction tank 10 is formed so as to span the upper end and the lower end of the reaction tank 10. Advanced Wastewater Treatment System. 제 3항 또는 제 4항에 있어서, 상기 반응조(10)의 바닥은 일측으로 경사면(11)이 형성되고, 경사면(11)에 산기장치(20)가 구비토록 됨을 특징으로 하는 생물막을 이용한 오ㆍ폐수의 고도처리장치.5. The biofilm using a biofilm according to claim 3 or 4, wherein the bottom of the reaction tank 10 is formed with an inclined surface 11 on one side, and an air diffuser 20 is provided on the inclined surface 11. Advanced Wastewater Treatment System.
KR1020020036429A 2002-06-27 2002-06-27 A way and a device to purify sevage and waste water by using a bed biofilm Ceased KR20040001286A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020020036429A KR20040001286A (en) 2002-06-27 2002-06-27 A way and a device to purify sevage and waste water by using a bed biofilm

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020020036429A KR20040001286A (en) 2002-06-27 2002-06-27 A way and a device to purify sevage and waste water by using a bed biofilm

Publications (1)

Publication Number Publication Date
KR20040001286A true KR20040001286A (en) 2004-01-07

Family

ID=37313054

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020020036429A Ceased KR20040001286A (en) 2002-06-27 2002-06-27 A way and a device to purify sevage and waste water by using a bed biofilm

Country Status (1)

Country Link
KR (1) KR20040001286A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102749233B1 (en) 2024-04-15 2024-12-31 현대엔지니어링 주식회사 Complex water treatment apparatus using membrane and biofilm

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR980001843A (en) * 1996-06-19 1998-03-30 유수 Downflow type microbial reactor for wastewater treatment
KR19980050066A (en) * 1996-12-20 1998-09-15 김정국 Simultaneous Removal of Organics, Nitrogen and Phosphorus in Wastewater by Using Fixed Biofilm Process and Bypass Flow
KR20000036316A (en) * 2000-01-10 2000-07-05 류종찬 Fluidized Media Biofilm Reactor with Clarifier
KR20010000876A (en) * 2000-10-25 2001-01-05 정명화 Internally-recycled aerobic biofilm reactor and the operation method of the reactor

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR980001843A (en) * 1996-06-19 1998-03-30 유수 Downflow type microbial reactor for wastewater treatment
KR19980050066A (en) * 1996-12-20 1998-09-15 김정국 Simultaneous Removal of Organics, Nitrogen and Phosphorus in Wastewater by Using Fixed Biofilm Process and Bypass Flow
KR20000036316A (en) * 2000-01-10 2000-07-05 류종찬 Fluidized Media Biofilm Reactor with Clarifier
KR20010000876A (en) * 2000-10-25 2001-01-05 정명화 Internally-recycled aerobic biofilm reactor and the operation method of the reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102749233B1 (en) 2024-04-15 2024-12-31 현대엔지니어링 주식회사 Complex water treatment apparatus using membrane and biofilm

Similar Documents

Publication Publication Date Title
EP2254842B1 (en) Method and device for the treatment of waste water
JPH02214597A (en) Device for nitrifying sewage
KR101292736B1 (en) Advanced wastewater treatment technology
JP5743448B2 (en) Sewage treatment equipment
KR101617426B1 (en) Advanced water-treating apparatus
KR100353004B1 (en) Biological Nutrient Removal Method using a Submerged Moving Media Intermittent Aeration Reactor and System
KR20040001286A (en) A way and a device to purify sevage and waste water by using a bed biofilm
JPH04367788A (en) Purification tank
KR101019092B1 (en) Advanced Wastewater Treatment System and Method for Phosphorus Removal
KR100473710B1 (en) Apparatus and method for disposing sewage with high accuracy
KR100519263B1 (en) Sewage treatment system
KR100342106B1 (en) Waste water treatment system of cross-flow anaerobic filter reactor by using recycled tire media and method using it
KR100862184B1 (en) Anaerobic or anoxic reactor employing density-controlled medias, apparatus and method for treating wastewater using the same
JP2002065106A (en) Rearing apparatus
KR102824775B1 (en) Nitrogen treatment process and device in wastewater using fixed biofilm reactor and fluidized biofilm reactor
KR200307954Y1 (en) Apparatus for disposing sewage with high accuracy
JPH05123696A (en) Biological nitrification and denitrification treatment equipment
JP2001070985A (en) Wastewater treatment equipment
JPH07163994A (en) Biological treating device of sewage
KR100521722B1 (en) Method of wastewater treatment using internal recyclein and step feeding
KR200237427Y1 (en) Disposal device of wastewater
KR20030036463A (en) Method for waste water treatment using float media
KR200344882Y1 (en) Advanced treatment system for removing nitrogen and phosphorus
JP3699706B2 (en) Sewage treatment equipment
JPH03296494A (en) Treatment apparatus for organic polluted water

Legal Events

Date Code Title Description
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 20020627

A201 Request for examination
PA0201 Request for examination

Patent event code: PA02012R01D

Patent event date: 20021024

Comment text: Request for Examination of Application

Patent event code: PA02011R01I

Patent event date: 20020627

Comment text: Patent Application

N231 Notification of change of applicant
PN2301 Change of applicant

Patent event date: 20021115

Comment text: Notification of Change of Applicant

Patent event code: PN23011R01D

PG1501 Laying open of application
E902 Notification of reason for refusal
PE0902 Notice of grounds for rejection

Comment text: Notification of reason for refusal

Patent event date: 20041013

Patent event code: PE09021S01D

E601 Decision to refuse application
PE0601 Decision on rejection of patent

Patent event date: 20050125

Comment text: Decision to Refuse Application

Patent event code: PE06012S01D

Patent event date: 20041013

Comment text: Notification of reason for refusal

Patent event code: PE06011S01I