KR20020011359A - Combination purifier tank - Google Patents

Combination purifier tank Download PDF

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Publication number
KR20020011359A
KR20020011359A KR1020010078013A KR20010078013A KR20020011359A KR 20020011359 A KR20020011359 A KR 20020011359A KR 1020010078013 A KR1020010078013 A KR 1020010078013A KR 20010078013 A KR20010078013 A KR 20010078013A KR 20020011359 A KR20020011359 A KR 20020011359A
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South Korea
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tank
aerobic
wastewater
sewage
carrier
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KR1020010078013A
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Korean (ko)
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KR100343257B1 (en
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성기달
이영호
김정목
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성기달
이영호
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • 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
    • C02F3/30Aerobic 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

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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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE: A combined wastewater/sewage treatment equipment is provided which effectively removes non-degradable organic pollutants including high concentrated organic materials, nitrogen and phosphorus contained in sewage and wastewater and has stable treatment capacities by connecting an aerobic fluidization tank and an aerobic contact tank in series. CONSTITUTION: In a combined wastewater/sewage treatment equipment in which an anaerobic sedimentation tank(3), an aerobic fluidization tank(4), an aerobic contact tank(5) and a clarifier(6) are sequentially formed between an inlet(1) into which sewage and wastewater are introduced and an outlet(2) through which purified sewage and wastewater are discharged, the combined wastewater/sewage treatment equipment comprises a baffle(11) which is installed in the aerobic fluidization tank(4); an air diffuser(12) for diffusing air which is arranged at the lower part between a separation plate(3a) between the aerobic fluidization tank(4) and the anaerobic sedimentation tank(3) and the baffle(11), and which is connected to an oxygen supplier(13); a suspending media(14) which is circulated in the aerobic fluidization tank(4); a fixed media(15) which is arranged in the central part of the aerobic contact tank(5); and an air diffuser(16) for diffusing air which is arranged between a separation plate(4a) between aerobic contact tank(5) and the aerobic fluidization tank(4) and the side surface of the fixed media(15), and which is connected to an oxygen supplier(13), wherein the suspending media(14) consists of a capsule made of a synthetic material on the surface of which a plurality of holes are formed, and which captures granular materials, a fixed filling material which is captured in the inner space of the capsule so as to be formed into a granular activated carbon that solidifies activated microorganisms, and a multifunctional filling material controlling an entire specific gravity.

Description

오·폐수 처리용 합병정화장치{COMBINATION PURIFIER TANK}Combined Purification System for Sewage and Wastewater Treatment {COMBINATION PURIFIER TANK}

본 발명은 일반 가정 및 식당 등의 영업장에서 발생되는 분뇨와 생활하수의 BOD, COD 등의 오염물질을 분해하는 합병정화장치에 관한 것으로, 특히 미생물(활성오니)를 유동상담체에 고정화하여 집적 배양되어 고농도의 활성미생물에 의한 호기성유동조 및 호기성접촉조를 직렬로 연결하는 구조로써 오,폐수에 포함되어 있는고농도의 유기물질, 질소, 인을 포함하는 난분해성 유기 오염물질 등의 제거 효율이 높고, 안정적인 처리능력을 가지는 오·폐수 처리용 합병정화장치에 관한 것이다.The present invention relates to a combined purification device that decomposes contaminants such as BOD and COD of manure and domestic sewage generated in the workplaces of general homes and restaurants, and in particular, microorganisms (active sludge) are immobilized on a fluid carrier to accumulate culture. It is a structure that connects aerobic flow tank and aerobic contact tank by high concentration of active microorganism in series, and it has high removal efficiency of high degradable organic pollutants including nitrogen, phosphorus The present invention relates to a combined purification apparatus for treating sewage and wastewater.

종래의 오수처리시설중의 정화조 시설은 일반적으로 혐기 및 호기성 접촉분해 방식의 처리방식으로서, 처리방법으로는 피처리물을 1차 처리로서 침전 및 혐기성미생물을 이용하여 분해시키고, 2차로 호기성 상태에서 고정상의 접촉담체를 이용하여 접촉 산화하는 방식을 많이 이용한 정화조를 사용하였다.In conventional sewage treatment facilities, septic tank facilities are generally anaerobic and aerobic catalytic cracking treatment methods. The treatment method is a first treatment to decompose the treated materials using sedimentation and anaerobic microorganisms, and in the second aerobic state. A septic tank using a lot of catalytic oxidation using a stationary phase carrier was used.

상기와 같은 정화조는 저농도의 오수 처리에는 일반적인 처리능력을 나타내고 있는데, 현재 영업장등에서의 오수는 농도 및 포함되는 오염물질이 난분해성을 포함하고 있기 때문에, 쉽게 처리할 수 없다는 문제점을 가지고 있다.The septic tank as described above shows a general treatment capacity for low concentration sewage treatment. Currently, septic tank has a problem in that it cannot be easily treated because sewage at the workplace or the like contains hardly decomposable concentrations.

또한 합병 정화조에 사용되는 담체는 여러 종류의 고정상 또는 유동상 시스템에 적용되는 담체가 개발되어 시판되고 있으나, 구조적 결함으로 인하여 물질 전달 및 유지관리면에서 관리의 어려움이 있어서 우수한 정화능력을 나타내지 못하고 있다.In addition, carriers used in combined septic tanks have been developed and marketed for various types of fixed bed or fluidized bed systems. However, due to structural defects, carriers have difficulty in management in terms of mass transfer and maintenance. .

특히 호기성 미생물을 이용하여 유기물을 분해하는 접촉조 등에서 고농도의 활성오니를 유지하기가 어려운 단점을 가지고 있다.In particular, it is difficult to maintain a high concentration of activated sludge in a contact tank for decomposing organic matter using aerobic microorganisms.

현재 고정상으로 설치하는 섬유상 담체를 살펴보면 이들은 비표면적을 크게한 섬유에 미생물이 부착하는 형태의 담체가 주류를 이루고 있으나, 이러한 담체는 유기물 등의 발생이 시간대별로 심한 편차를 나타내는 특징을 가지는 오수의 처리에 있어서 전단응력에 의한 물리적 힘에 의하여 탈리가 쉽게 되고 부하변동에 대한대응력이 약한 문제점을 가지고 있다.When looking at the fibrous carriers installed in the stationary phase, they are mainly the carriers in which microorganisms adhere to the fibers having a large specific surface area, but these carriers are characterized by the treatment of sewage, which is characterized by severe variation in time of generation of organic matter. Desorption is easy due to the physical force caused by shear stress, and the stress against load fluctuation is weak.

현재 합병 정화조의 처리효율이 떨어지는 가장 큰 두가지 원인을 가지고 있는데, 이는 첫째 생활 및 영업장의 오 폐수 등이 난분해성 물질을 함유하고 있으며, 두 번째는 오폐수의 농도별 및 발생시간대별 편차가 매우 심하기 때문이다.Currently, there are two main causes of the poor treatment efficiency of merged septic tanks: First, wastewater from living and business places contain hardly decomposable substances, and secondly, the variation of wastewater by concentration and generation time is very severe. to be.

오, 폐수의 처리에 있어서 생물공학적인 방법은 오폐수 중의 오염물질을 미생물의 신진대사에 필요로 하는 기질로 이용하는 방식인데, 오폐수의 농도 및 발생이 편차가 심하기 때문에 미생물의 활성을 유지하기 매우 힘든 실정이다.The biotechnological method in the treatment of wastewater is to use the pollutants in the wastewater as substrates required for the metabolism of microorganisms, and it is very difficult to maintain the activity of microorganisms because the concentration and occurrence of wastewater are severe. to be.

또한 난분해성 유기물질의 영향을 살펴보면, 난분해성 물질을 분해 섭취하는 미생물이 증식속도가 대단히 느리기 때문에 미생물의 부착 및 탈리가 쉬운 담체로 접촉하는 정화조에서는 난분해성 물질의 분해능을 가진 미생물이 고정화하기 어렵다.In addition, the effects of the hardly decomposable organic substances show that the microorganisms having the ability to decompose the hardly decomposable substances are difficult to be immobilized in the septic tank contacted with a carrier which is easy to attach and detach the microorganisms because the microorganisms that decompose and ingest the hardly decomposable substances are extremely slow in growth. .

본 발명은 상기와 같은 종래 기술의 이러한 문제점을 극복하여 안정적이면서 우수한 처리효율로 오폐수를 처리하기 위한 발명의 목적을 달성하기 위하여, 심한 부하변동에 대응이 강한 시스템, 질소의 효과적인 제거, 세제를 포함하는 난분해성 물질의 효과적인 제거, 고농도의 유기성 오염물질의 효과적인 제거를 과제로 한다.The present invention overcomes these problems of the prior art as described above, in order to achieve the object of the invention for treating wastewater with a stable and excellent treatment efficiency, a system that is resistant to severe load fluctuations, effective removal of nitrogen, detergents The present invention aims to effectively remove hardly decomposable substances and to remove high concentrations of organic contaminants.

즉 본 발명의 목적은 합병 정화장치에서 유기물질 및 질소 인을 효과적으로 제거하기 위해서는 고농도의 고정화 미생물을 이용한 처리방식을 도입하는 방안과 더불어 물질 및 산소 전달 및 적정한 미생물 고정화의 농도를 유지하기 위한 방안으로 고활성을 계속적으로 유지할 수 있는 담체를 이용하여 이를 생물공학적인 처리시설에 적절히 적용하여 우리나라 실정에 맞으면서 안정적인 처리효율을 나타내는 합병 정화장치를 제공하는 데 있다.That is, an object of the present invention is to introduce a treatment method using a high concentration of immobilized microorganisms in order to effectively remove organic substances and nitrogen phosphorus from the combined purification device, as well as a method for maintaining the concentration of the substance and oxygen transfer and proper microorganism immobilization. By using a carrier that can continuously maintain high activity, it is appropriately applied to a biotechnological treatment facility to provide a merger purifier that meets the situation of Korea and shows stable treatment efficiency.

본 발명은 오수와 폐수를 유입하는 유입구와 정화 처리된 오수와 폐수를 유출하는 유출구 사이에 침전혐기조, 호기성유동조, 호기성접촉조, 침전조를 순차적으로 형성하여 오수와 폐수를 처리하는 합병정화장치에 있어서, 호기성유동조에 배플이 설치되고, 상기 호기성유동조와 침전혐기조 사이의 격판과 배플 사이의 하부에서 공기를 분사하는 산기구가 배치되어 산소공급기와 연결됨과 더불어 유동상담체가 상기 호기성유동조에서 순환 운동하게 되며, 호기성접촉조의 중앙부에 고정상담체를 배치함과 더불어 상기 호기성접촉조와 호기성유동조 사이의 격판과 고정상담체의 측면 사이에서 공기를 분사하는 산기구가 배치되어 상기 산소공급기와 연결되는 것을 포함하되, 상기 유동상담체는 표면에 다수의 구멍을 형성함과 더불어 입상물질을 포획하는 합성수지 재질의 캡슐, 상기 캡슐의 내부 공간에 포획되어 활성 미생물을 고정화한 입상활성탄으로 형성된 고정화충진물질, 그리고 전체의 비중을 조절하는 다기능성충진물질로 이루어지는 오·폐수 처리용 합병정화장치를 제공한다.In the present invention, a sedimentation anaerobic tank, aerobic flow tank, aerobic contact tank, and sedimentation tank are sequentially formed between an inlet for introducing sewage and wastewater and an outlet for purifying treated sewage and wastewater. In the aerobic flow tank, a baffle is installed, and an acid mechanism for injecting air from the lower portion between the diaphragm and the baffle between the aerobic flow tank and the settling anaerobic tank is arranged and connected to an oxygen supply, and the fluid carrier is circulated in the aerobic flow tank. In addition, the stationary carrier is disposed at the center of the aerobic contacting tank, and an air diffuser for injecting air between the side of the diaphragm and the fixed carrier between the aerobic contacting tank and the aerobic fluidizing tank is disposed to be connected to the oxygen supply device. Including, but the fluid carrier to form a plurality of holes on the surface and capture the particulate matter Provides a composite purification device for sewage and wastewater treatment consisting of a synthetic resin capsule, an immobilized filler formed of granular activated carbon trapped in the inner space of the capsule and immobilized active microorganisms, and a multifunctional filler that controls the specific gravity of the whole. do.

도 1은 본 발명에 의한 오·폐수 처리용 합병정화장치의 단면도,1 is a cross-sectional view of the combined purification device for wastewater treatment according to the present invention,

도 2는 본 발명에 의한 합병정화장치의 호기성유동조의 모형도,Figure 2 is a model of the aerobic flow tank of the combined purification apparatus according to the present invention,

도 3은 본 발명에 의한 합병정화장치의 호기성접촉조의 모형도이다.3 is a model diagram of an aerobic contact tank of the combined purification apparatus according to the present invention.

<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>

11 : 배플11: baffle

12, 16 : 산기구12, 16: acid diffuser

13 : 산소공급기13 oxygen supply

14 : 유동상담체14: flow counseling

15 : 고정상담체15: fixed consultation

이하 본 발명의 바람직한 실시예를 첨부한 도면에 의거하여 더욱 상세하게 설명한다.Hereinafter, preferred embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

도 1은 본 발명에 의한 오·폐수 처리용 합병정화장치를 나타내는 도면으로서, 오수와 폐수를 유입하는 유입구(1)와 정화 처리된 오수와 폐수를 유출하는 유출구(2) 사이에 침전혐기조(3), 호기성유동조(4), 호기성접촉조(5), 침전조(6)를 순차적으로 형성하게 된다.1 is a view showing a combined purification and purification apparatus for wastewater treatment according to the present invention, wherein a sedimentation anaerobic tank 3 is disposed between an inlet 1 for introducing sewage and wastewater and an outlet 2 for discharging purified sewage and wastewater. ), The aerobic flow tank (4), aerobic contact tank (5), the precipitation tank (6) will be formed sequentially.

그리고 본 발명은 상기 호기성유동조(4)에 설치되는 배플(baffle)(11), 상기 호기성유동조(4)와 침전혐기조(3) 사이의 격판(3a)과 상기 배플(11) 사이의 하부에 배치되는 산기구(12), 상기 산기구(12)에 공기를 공급하는 산소공급기(13), 상기 호기성유동조(4)에 내장되는 유동상담체(14), 상기 호기성접촉조(5)의 중앙부에 배치되는 고정상담체(15), 그리고 상기 호기성접촉조(5)와 호기성유동조(4) 사이의 격판(4a)과 상기 고정상담체(15)의 측면 사이의 하부에 배치되어 상기 산소공급기(13)와 연결되는 산기구(16)로 이루어진다.And the present invention is a baffle (11) installed in the aerobic flow tank (4), the diaphragm (3a) between the aerobic flow tank (4) and sedimentation anaerobic tank (3) and the lower portion between the baffle (11) An air diffuser 12 disposed in the air supply unit, an oxygen supplier 13 for supplying air to the air diffuser 12, a fluid carrier 14 embedded in the aerobic flow tank 4, and the aerobic contacting tank 5 A fixed carrier 15 disposed at the center of the diaphragm, and a diaphragm 4a between the aerobic contacting tank 5 and the aerobic fluidizing tank 4 and a lower side between the side of the fixed carrier 15 and It consists of a diffuser (16) connected to the oxygen supply (13).

특히 상기 유동상담체(14)는 도 4에 도시한 바와 같이, 표면에 다수의 구멍을 형성함과 더불어 입상물질을 포획하는 합성수지 재질의 다공질 캡슐(14a), 상기 캡슐(14a)의 내부 공간에 포획되어 활성 미생물을 고정화한 입상활성탄으로 형성된 고정화충진물질(14b), 그리고 전체의 비중을 조절하는 다기능성충진물질(14c)로 이루어진다.In particular, as shown in FIG. 4, the fluid carrier 14 is formed in a porous capsule 14a made of a synthetic resin material which traps particulate matter and traps granular material, and is formed in the interior space of the capsule 14a. It consists of an immobilized filler material 14b formed of granular activated carbon obtained by trapping and immobilizing active microorganisms, and a multifunctional filler material 14c for adjusting the specific gravity of the whole.

즉 본 발명은 고농도의 기질에 순화되어 우수한 오염물질의 제거능을 가진 미생물을 입상활성탄의 마이크로포어(micropore)또는 매소포어(mesopore)내에 포획한 형태의 고정화충진물질(14b)을 제조한 뒤, 상기 고정화충진물질(14b)과 함께 상기 다기능성충진물질(14c)을 다공질의 캡슐(14a)에 충진하게 되며, 완전 혼합형의 호기성유동조(4) 및 고정상담체(15)를 이용한 호기성접촉조(5)를 직렬로 연결한 것이다.That is, according to the present invention, after the microorganism having a high concentration of substrate is purified and trapped in the micropore or mesopore of granular activated carbon, the immobilized filler 14b is prepared. The multifunctional filling material 14c together with the immobilizing filling material 14b is filled into the porous capsule 14a, and an aerobic contacting tank using the fully mixed aerobic fluid tank 4 and the fixed carrier 15 5) is connected in series.

상기 산기구(12)는 도 2에 도시한 바와 같이, 산소공급기(13)의 압축 공기를 분사함으로써 유출되는 공기가 상기 격판(3a)과 상기 배플(11) 사이의 하부에서 위쪽 방향으로 상승되어 상기 유동상담체(14)가 상기 호기성유동조(4) 내부에서 원활하게 순환하게 된다.As shown in FIG. 2, the air diffuser 12 is discharged from the lower portion between the diaphragm 3a and the baffle 11 upwards by injecting the compressed air of the oxygen supplier 13. The fluid carrier 14 is circulated smoothly in the aerobic fluid tank 4.

상기 산기구(16)는 도 3에 도시한 바와 같이, 산소공급기(13)의 압축공기를 분사함으로써 유출되는 공기가 상기 격판(4a)과 고정상담체(15) 사이의 하부에서 위쪽 방향으로 상승되어 상기 호기성접촉조(5) 내의 오수와 폐수를 고정상담체(15)와 원활하게 접촉시킨다.As shown in FIG. 3, the air diffuser 16 ascends from the lower portion between the diaphragm 4a and the fixed carrier 15 upwards from the air flowing out by spraying compressed air of the oxygen supplier 13. Thus, the sewage and wastewater in the aerobic contacting tank 5 are brought into smooth contact with the fixed carrier 15.

물론 본 발명에서는 종래와 마찬가지로 상기 침전조(6)의 최하부에 순환펌프(7)를 설치하여 침전조(6)에 가라앉은 오수와 폐수를 상기 침전협기조(3)로 리턴하게 되고, 상기 침전협기조(3)에 협기성담체(8)를 배치함은 자명하다.Of course, in the present invention, the circulating pump 7 is installed at the bottom of the settling tank 6 to return the sewage and wastewater submerged in the settling tank 6 to the settling cooper tank 3, as described above. It is obvious to place the anaerobic carrier 8 in (3).

이 때 본 발명에 의한 합병정화장치의 호기성접촉조(5)에 사용된 고정상담체(15)는 활성 미생물을 포획하는 구조의 상기 유동상담체(14)에 사용된 고정화충진물질(14b)을 채운 것을 사용하고, 호기성유동조(4)에 사용된 유동상담체(14)는 활성미생물을 포획하는 구조의 고정화충진물질(바이오파티클TM)(14b)을 다기능성충진물질(14c)과 혼합하여 만든다.At this time, the fixed carrier 15 used in the aerobic contacting tank 5 of the combined purification apparatus according to the present invention is the immobilized filling material 14b used in the fluid carrier 14 of the structure to capture the active microorganisms. The fluid carrier 14 used in the aerobic flow tank 4 using the filled material is mixed with a multifunctional filler 14c by immobilizing a filler (bioparticle TM ) 14b having a structure for trapping active microorganisms. Make.

여기서 고정화충진물질(14b)의 비중은 1.4 정도로서 물보다 무겁기 때문에, 호기성유동조(4)에서는 완전 혼합형 상태의 유동이 가능하게 하기 위하여 특별히 다기능성충진물질(바이오볼TM)(14c)을 제조하여 고정화충진물질(14b)과 적정비율로혼합하여 유동상담체(14)를 만들게 된다.Here, since the specific gravity of the immobilized filler material 14b is about 1.4, which is heavier than water, the aerobic fluid tank 4 specifically prepares a multifunctional filler material (bioball TM ) 14c to enable flow in a completely mixed state. It is mixed with the immobilized filling material (14b) in an appropriate ratio to form a fluid carrier (14).

물론 호기성접촉조(5)에 사용하는 고정상담체(일명 바이오카트리지TM라고도 함)에 대해서 설명하면 원기둥형, 직사각형, 무정형 등 접촉조에 설치가 용이한 형태의 다공질의 포획체에 별도 미생물 배양장치에서 배양된 우수한 오염물질 제거능력을 가진 미생물을 고정화된 고정화충진물질(바이오파티클TM)을 충진해서 사용하고, 호기성유동조(4)에 사용되는 유동상담체(바이오캡슐TM)는 구형의 형태를 가지는 다공질의 캡슐(14a)에 고정상담체에 사용하는 미생물을 고정화된 고정화충진물질(14b)(일명 바이오파티클TM이라고도 함)과 비중 조절을 위한 다기능성충진물질(14c)(일명 바이오볼TM이라고 함)을 혼합하여 충진하는 구조로 제작한다.Of course, the fixed carrier used in the aerobic contact tank 5 (also referred to as biocartridge TM ) will be described in a separate microbial culture apparatus in a porous capture body that is easy to install in a contact tank such as a cylinder, a rectangle, and an amorphous form. The microorganisms with excellent pollutant removal ability are cultured and filled with immobilized immobilization fillers (Bioparticles TM ), and the fluid carriers (Biocapsules TM ) used in the aerobic flow tank 4 have a spherical shape. The microorganisms used for the fixed carriers in the porous capsule 14a are immobilized immobilization material 14b (also called bioparticles TM ) and multifunctional fillers 14c for specific gravity control (also called bioballs TM ). ) Is manufactured by mixing and filling.

여기서 포획체와 캡슐(14)의 재질는 프라스틱류, 철재류, 섬유소재류 등을 모두 사용할 수 있으나, 고정상담체(15)에서는 체망의 P.P 섬유소재, 유동상담체(14)에서는 물질 및 산소전달이 용이한 구조의 프라스틱 소재가 바람직하며, 또 유동상담체(14)는 다기능성충진물질(14c)의 충진비율을 조절하여, 비중의 조절이 가능하여, 오 폐수중에서 잘 유동될 수 있도록 할 수 있는 기능을 부여하게 된다.The capturing body and the capsule 14 may be made of plastics, iron materials, fiber materials, etc., but the fixed carrier 15 may be a PP fiber material of the sieve network, and the fluid carrier 14 may easily transfer materials and oxygen. The plastic material of one structure is preferable, and the fluid carrier 14 controls the filling ratio of the multifunctional filling material 14c, so that the specific gravity can be controlled, so that the fluid can flow well in the wastewater. Will be given.

다기능성충진물질(14c)의 비중은 0.35 - 0.45로서 그의 물리화학적 성질이 매우 우수하며, 미립 활성탄을 소재로 하여 발포제를 사용하여 비중이 가벼운 담체를 만들기 때문에 비표면적이 평균 1,500n/g으로서 매우 크며, 비중 조절은 물론 많은 미생물이 고정화 할 수 있는 다기능성을 가지게 된다.The specific gravity of the multifunctional filler (14c) is 0.35-0.45, and its physical and chemical properties are very excellent, and the specific surface area is 1,500 n / g because the specific gravity of the activated carbon is used to make the carrier with the specific gravity. It is large, and it has a multifunctionality that can be immobilized as well as specific gravity control.

또한 본 발명에 의한 다기능성충진물질(14c)의 비율을 조절함으로서 완전 혼합형 반응기에 사용될 담체 , 충진형 반응기용 담체, 부상형 반응기에 사용될 담체 등 마음대로 조절할 수가 있다.In addition, by adjusting the ratio of the multifunctional filler material (14c) according to the present invention can be adjusted at will, such as a carrier to be used in a completely mixed reactor, a carrier for a filling reactor, a carrier to be used in a floating reactor.

이 때 오폐수를 처리하는 시스템의 종류별 필요한 담체의 비중에 관하여 알아보면 아래의 표 1과 같은데, 이러한 담체를 만들고자 할 때 본 발명에 사용되는 유동상담체(14)는 다기능성충진물질의 비율을 조절함으로써 모든 반응기에 사용 가능한 다기능성을 보유한다.At this time, the specific gravity of the carrier required for each type of wastewater treatment system is as shown in Table 1 below, when making the carrier, the fluid carrier 14 used in the present invention controls the ratio of the multifunctional filler material. Thereby retaining the versatility available for all reactors.

반응기 종류Reactor type 비 중importance 완전혼합형 반응기용For fully mixed reactor 0.98-1.030.98-1.03 충진형 반응기용For filling reactors 1.20 이상1.20 or more 부상형 반응기용For floating reactor 0.98 이하0.98 or less

본 발명에 의한 합병정화장치는 호기성유동조(4)에서 유동상담체(14)를 이용하여 완전 혼합 형태의 반응기에서 유기물질등의 오염물질을 완전히 분해하고, 여기서 미처리된 유기물질 및 유동상에서 탈리된 미생물을 포함하는 현탁물질을 호기성접촉조(5)에서 흡착 및 생물학적으로 처리하여 오,폐수의 오염물질을 완전히 정화 처리하게 된다.The combined purification apparatus according to the present invention completely decomposes contaminants such as organic substances in a fully mixed reactor by using the fluid carrier 14 in the aerobic flow tank 4, and desorbs from the untreated organic substances and the fluidized bed. Suspended material containing the microorganisms is adsorbed and biologically treated in the aerobic contact tank (5) to completely clean the contaminants of the wastewater.

고정상담체(15)는 미생물을 고정화한 고정화충진물질을 10메쉬(mesh)의 구멍 크기의 섬유를 고정상으로 설치가 용이한 원기둥 형태가 되도록 충진하여 만들어 도 3과 같이 되도록 호기성접촉조(5)에 고정화하고, 유동상담체(14)의 형태는 10메쉬(mesh)크기의 구멍을 보유한 플라스틱 재질의 다공질 캡슐(14a) 내부에 활성미생물을 포획한 고정화충진물질(14b)과 다기능성충진물질(14c)을 채운 것으로서, 유동상담체(14)의 물리화학적 성질을 살펴보면 아래의 표 2와 같다The fixed carrier 15 is filled with an immobilized filler material immobilized with microorganisms into a cylindrical shape that is easy to install with a fiber having a pore size of 10 mesh. The immobilized filler material 14b and the multifunctional filler material having the active microorganisms trapped inside the porous capsule 14a made of plastic material having a hole of 10 mesh size, 14c), the physical and chemical properties of the fluid carrier 14 is shown in Table 2 below.

번호number 분석항목Analysis item 분석결과Analysis 단위unit 1One Wet densityWet density 1.011.01 g/cm3 g / cm 3 22 겉보기 밀도Apparent density 1.201.20 g/cm3 g / cm 3 33 직경diameter 4.54.5 cmcm 44 미생물량Microbial mass 3535 g/EAg / EA

상기와 같이 이루어지는 합병정화장치는 침전혐기조(3)에서 오수와 폐수의 침전물질 및 유기물을 제거하고, 호기성유동조(4)의 유동상담체(14)와 호기성접촉조(5)의 고정상담체(15)를 사용하여 용이하게 정화 처리하게 된다.The combined purification apparatus as described above removes sediment and organic matter of sewage and wastewater from the settling anaerobic tank 3, and fixes the fixed carrier of the fluid carrier 14 and the aerobic contacting tank 5 of the aerobic flow tank 4. Purification treatment is easily performed using (15).

오수, 폐수 등과 같은 피처리물질은 유입구(1)로 침전혐기조(3)로 유입되면 입자상 물질은 침전이 되고, 유기물질 등의 오염물질이 혐기성담체(8)에 부착된 미생물 등에 의하여 1차로 혐기분해가 이루어지고, 격판(3a)을 월류하여 호기성유동조(4)에 유입된다.When treated materials such as sewage and waste water enter the sedimentation anaerobic tank (3) through the inlet (1), particulate matter precipitates, and the first anaerobic anaerobic microorganisms are attached to the anaerobic carrier (8). Decomposition takes place and the diaphragm 3a flows over and flows into the aerobic flow tank 4.

호기성유동조(4)에 유입된 피처리물의 오염물질은 유동상담체(14)에 고정화된 고활성 미생물에 의해서 분해되고, 질소 성분은 담체의 내부 혐기영역으로 분자 이동되어 탈질된다.The contaminants of the workpieces introduced into the aerobic flow tank 4 are decomposed by the highly active microorganisms immobilized on the fluid carrier 14, and the nitrogen component is molecularly moved to the internal anaerobic region of the carrier for denitrification.

이 때 필요한 산소는 산기관(12), 산소공급기(13)에 의해 공급되고, 유동상담체(14)의 유동은 배플(11)의 도움을 받아, 도 2에 도시한 바와 같이 호기성유동조(4)에 완전혼합형의 생물반응기의 모델로 유동되어 산소, 활성미생물 및 오염물질의 전달이 용이해지게 된다.At this time, the necessary oxygen is supplied by the diffuser 12 and the oxygen supplier 13, and the flow of the fluid carrier 14 is assisted by the baffle 11, as shown in FIG. 4) flows into the model of a fully mixed bioreactor to facilitate the transfer of oxygen, active microorganisms and contaminants.

여기서 일정 시간 처리된 피처리물질은 유동상담체(14)가 통과하지 못하는 구조의 체망의 구조형식의 월류웨어 장치로 구성된 격판(4a)을 넘어 호기성접촉조(5)에 이르게 된다.Here, the material to be treated for a certain time reaches the aerobic contact tank 5 beyond the diaphragm 4a constituted by the overflowware device of the structural type of the network of the structure in which the fluid carrier 14 cannot pass.

여기에서 그 동안 미처리된 잔류 오염물질 및 현탁물질이 활성고정화된 고정상담체(15)에 흡착 분해되어 완전히 정화되며, 정화 처리된 피처리물은 호기성접촉조(5)와 침전조(6) 사이의 격판을 지나 침전조(6)로 이동되어, 일정시간 정체되어 침전된 활성오니는 순환펌프(7)에 의해 침전협기조(3)로 리턴됨과 더불어 깨끗한 상등액은 유출구(2)를 통하여 방류된다.Here, the untreated residual contaminants and suspended substances are adsorbed and decomposed to the fixed and fixed carriers 15 which are activated and completely purified, and the purified to-be-processed object is disposed between the aerobic contacting tank 5 and the settling tank 6. The activated sludge, which is moved to the settling tank 6 through the diaphragm and is settled for a predetermined time, is returned to the settling tank 3 by the circulation pump 7 and the clean supernatant is discharged through the outlet 2.

본 발명에 의한 합병정화장치의 성능을 고찰하기 위해 식당오수를 처리하는 실험을 하였다.In order to examine the performance of the combined purification apparatus according to the present invention, an experiment was conducted to treat restaurant sewage.

이 때 처리조건은 체류시간 24시간을 유지하였으며, 시험기간은 1999.4.1 - 1999. 6. 30까지 약 3개월 연속 시험하였다. 연속시험결과 표 3과 같고, 이 때 유입수 및 유출수의 분석은 매일 1회 실시하였으며, 분석방법은 Standard method 에 준하여 분석하였다.At this time, the treatment condition was maintained for 24 hours, and the test period was tested for about 3 months from 1999.4.1-June 30, 1999. The results of the continuous test are shown in Table 3, where the influent and the effluent were analyzed once daily, and the analysis method was analyzed according to the standard method.

측정항목Metric 유입수Influent 유출수Runoff 평균제거효율Average removal efficiency 농 도Concentration 평 균Average 농 도Concentration 평 균Average BODBOD 450-800450-800 650650 8-138-13 1010 98%98% CODcrCODcr 320-920320-920 780780 15-2515-25 2020 97%97% SSSS 30-28030-280 150150 6-106-10 88 95%95% TKNTKN 20-6020-60 3636 4이하4 or less 22 94%94%

표 3의 시험결과표에 나타난 바와 같이 식당의 오수가 과량의 세제등의 난분해성을 포함하면서 오염물질의 농도가 BOD가 평균 650mg/L, COD가 평균 780mg/L ,등 매우 높은 농도임에도 BOD의 제거효율이 BOD 98%, COD 97%, SS 95%, TKN 94%등으로 매우 우수한 제거능력을 발휘하였다.As shown in the test results table of Table 3, BOD removal is very high even though the concentration of contaminants is very high such as BOD average 650mg / L, COD average 780mg / L, etc. The efficiency was very good with 98% BOD, 97% COD, 95% SS and 94% TKN.

본 발명에 의한 호기성유동조와 호기성접촉조에서 연속 처리하는 합병정화장치는 오수처리에 있어서 매우 효과적으로 오염물질을 처리하여 매우 안정적인 처리수질을 얻을 수 있으며, 상수도 보호지역 내의 식당오수등을 처리하는 데 적합하며, 하수처리가 불가능한 지역의 생활오수를 처리하기 위해 설치하면 매우 우수한 처리능으로 인하여 자연 환경 보존에 크게 기여하는 효과를 제공한다.The combined purification apparatus for continuous treatment in aerobic flow tank and aerobic contact tank according to the present invention can treat pollutants very effectively in sewage treatment to obtain very stable treated water quality, and is suitable for treating restaurant sewage in waterworks protected areas. In addition, when installed to treat domestic sewage in areas where sewage treatment is impossible, it provides an effect that greatly contributes to the preservation of the natural environment due to its excellent treatment ability.

Claims (1)

오수와 폐수를 유입하는 유입구와 정화 처리된 오수와 폐수를 유출하는 유출구 사이에 침전혐기조, 호기성유동조, 호기성접촉조, 침전조를 순차적으로 형성하여 오수와 폐수를 처리하는 합병정화장치에 있어서,In the combined purification apparatus for treating sewage and wastewater by sequentially forming a sedimentation anaerobic tank, aerobic flow tank, aerobic contact tank, and sedimentation tank between an inlet for introducing sewage and wastewater and an outlet for purifying treated sewage and wastewater, 호기성유동조에 배플이 설치되고, 상기 호기성유동조와 침전혐기조 사이의 격판과 배플 사이의 하부에서 공기를 분사하는 산기구가 배치되어 산소공급기와 연결됨과 더불어 유동상담체가 상기 호기성유동조에서 순환 운동하게 되며, 호기성접촉조의 중앙부에 고정상담체를 배치함과 더불어 상기 호기성접촉조와 호기성유동조 사이의 격판과 고정상담체의 측면 사이에서 공기를 분사하는 산기구가 배치되어 상기 산소공급기와 연결되는 것을 포함하되,A baffle is installed in the aerobic flow tank, and an acid mechanism for injecting air from the lower portion between the diaphragm and the baffle between the aerobic flow tank and the settling anaerobic tank is arranged to be connected to an oxygen supply, and the fluid carrier is circulated in the aerobic flow tank. In addition, the stationary carrier is disposed at the center of the aerobic contacting tank, and an air diffuser for injecting air between the side of the diaphragm and the fixed carrier between the aerobic contacting tank and the aerobic fluidizing tank is arranged to be connected to the oxygen supply. , 상기 유동상담체는 표면에 다수의 구멍을 형성함과 더불어 입상물질을 포획하는 합성수지 재질의 캡슐, 상기 캡슐의 내부 공간에 포획되어 활성 미생물을 고정화한 입상활성탄으로 형성된 고정화충진물질, 그리고 전체의 비중을 조절하는 다기능성충진물질로 이루어지는 오·폐수 처리용 합병정화장치.The fluid carrier is formed of a synthetic resin capsule that traps granular material and forms a plurality of pores on the surface, an immobilized filler formed of granular activated carbon trapped in the inner space of the capsule to immobilize the active microorganism, and the specific gravity of the whole. Combined purification device for wastewater treatment consisting of multifunctional filling material to control the.
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CN103193321A (en) * 2013-05-03 2013-07-10 哈尔滨工业大学 Sludge self-circulation dispersed sewage treatment device applicable to directly-discharged water body and method thereof
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