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 PDFInfo
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- 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
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- 239000002351 wastewater Substances 0.000 title claims description 13
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 12
- 238000001914 filtration Methods 0.000 claims description 8
- 239000000969 carrier Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 6
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 230000007423 decrease Effects 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000010802 sludge Substances 0.000 description 9
- 239000012530 fluid Substances 0.000 description 6
- 244000005700 microbiome Species 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 208000012868 Overgrowth Diseases 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000295 complement effect Effects 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000002062 proliferating effect Effects 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/06—Aerobic processes using submerged filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/08—Aerobic processes using moving contact bodies
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
- C02F3/1273—Submerged membrane bioreactors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1278—Provisions for mixing or aeration of the mixed liquor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/20—Activated sludge processes using diffusers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- 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
Description
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.
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| 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 |
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| 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 |
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| KR102749233B1 (en) | 2024-04-15 | 2024-12-31 | 현대엔지니어링 주식회사 | Complex water treatment apparatus using membrane and biofilm |
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