KR20020092877A - Wastewater Treatment Apparatus using Internal Recycle in ICEAS - Google Patents

Wastewater Treatment Apparatus using Internal Recycle in ICEAS Download PDF

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KR20020092877A
KR20020092877A KR1020020069742A KR20020069742A KR20020092877A KR 20020092877 A KR20020092877 A KR 20020092877A KR 1020020069742 A KR1020020069742 A KR 1020020069742A KR 20020069742 A KR20020069742 A KR 20020069742A KR 20020092877 A KR20020092877 A KR 20020092877A
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South Korea
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sludge
wastewater
reactor
wastewater treatment
sewage
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KR1020020069742A
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Korean (ko)
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황종열
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세림제지주식회사
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Priority to KR1020020069742A priority Critical patent/KR20020092877A/en
Publication of KR20020092877A publication Critical patent/KR20020092877A/en

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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
    • C02F3/12Activated sludge processes
    • C02F3/1205Particular type of activated sludge processes
    • C02F3/1221Particular type of activated sludge processes comprising treatment of the recirculated sludge
    • 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
    • C02F3/1284Mixing devices
    • 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
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/22Activated sludge processes using circulation pipes
    • 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

Abstract

PURPOSE: An intermittent cycle extended aeration system of internal recycle type for sewage/wastewater treatment is provided, which is characterized in that sludge of a secondary reactor is recycled into a primary reactor through a sludge recycle pipe line. Therefore contact time of bacteria of sludge and organics is increased, and removal efficiency of organics, nitrogen, and phosphorus is improved. CONSTITUTION: The system comprises a primary reactor(4), a secondary reactor(2) for treating sewage/wastewater. Air for bacteria growth is supplied by an air supply valve(5). Sludge of the secondary reactor(2) is recycled into the primary reactor(4) through a sludge pump(12), a valve(15), and the sludge recycle pipe line(14). The system uses bacteria of sludge repeatedly by recycle, so treatment efficiency is improved.

Description

내부반송형 간헐주기장기폭기식 하,폐수처리장치 {Wastewater Treatment Apparatus using Internal Recycle in ICEAS}Wastewater Treatment System for Internal Transfer Type Intermittent Long-term Aeration Type {Wastewater Treatment Apparatus using Internal Recycle in ICEAS}

본 발명은 도시하수 및 산업폐수등의 하,폐수를 고도로 정화처리 하기 위하여 종래의 간헐주기장기폭기법(Intermittent Cycle Extended Aeration System :ICEAS)인 소위 이키아스(ICEAS)공법에 의한 하,폐수처리장치에서 슬러지의 반복반송에 의한 재활용으로 미생물활성을 증가시켜 하,폐수의 유기물, 질소 및 인의 제거효율향상으로 하,폐수의 효과적인 정화처리가 될 수 있도록 하,폐수가 정화처리 제1단계인 전반응조를 거쳐서 제2단계인 주반응조에 유입되었을 때,The present invention is a sewage and wastewater treatment apparatus according to the so-called ICEAS method, which is a conventional Intermittent Cycle Extended Aeration System (ICEAS) in order to purify sewage and wastewater such as urban sewage and industrial wastewater. Recycling by repetitive transport of sludge to increase the efficiency of removing organic matter, nitrogen and phosphorus from sewage and wastewater, and to effectively purify wastewater and wastewater. When introduced into the main reactor, the second stage through

하수중의 호기성 미생물이 폭기공기와 혼합하여 하수중의 유기오탁물을 분해,산화하며 증식하여 형성된 슬러지를 정화처리 제1단계인 전반응조로 되돌려 보내기 위한 슬러지내부반송파이프라인을 설치한 것을 특징으로 하는 내부반송형 간헐주기장기폭기식 하,폐수처리 장치에 관한 것이다.Sludge internal transport pipeline is installed to return sludge formed by aerobic microorganisms in sewage to aerated air by decomposing, oxidizing and multiplying organic contaminants in sewage. It relates to an internal transport type intermittent long-term aeration type wastewater treatment device.

일반적으로 폭기식 하,폐수 처리장치는 하,폐수를 공기로 폭기혼합하면 여러가지 호기성미생물이 증식하게되며 유기,무기의 부유고형물과 응집하여 침강성이 좋은 활성슬러지가 형성되어, 최종침전조인 주반응조에서 하,폐수중의 유기오탁물질을 분해,산화하여 청정한 처리수만을 처리수유출장치인 디캔터(Decanter)를 통하여 유출시키는 것으로서,현재 세계적으로 가장 널리 쓰여지고 있는 하,폐수처리장치이다.In general, aeration type wastewater treatment device is aeration mixed wastewater and wastewater with air, and various aerobic microorganisms multiply and aggregate with organic and inorganic suspended solids to form activated sludge with good sedimentation. It is a sewage and wastewater treatment device that is used most widely in the world at present as it decomposes and oxidizes organic pollutants in wastewater and discharges only clean water to be treated through a decanter.

종래에는 상기한 폭기식 하,폐수처리장치에서 하수를 정화처리 제1단계인 전반응조를 통하여 주반응조로 보낸후 공기공급밸브에서 공기를 공급하여 폭기혼합하여 미생물의 활성으로 하수를 정화하고 침강한 활성슬러지중 슬러지를 슬러지펌프로 펌핑수거하여 슬러지외부배출파이프라인을 통하여 폐기시켰다.Conventionally, in the aeration type wastewater treatment device, the sewage is sent to the main reaction tank through the pre-reactor, which is the first step of the purification process, and then air is supplied from the air supply valve to mix the aeration to purify the sewage with the activity of microorganisms and settle. The sludge in the activated sludge was pumped into the sludge pump and discarded through the sludge external discharge pipeline.

본 발명은 종래의 주반응조에서 하수를 정화처리하고 침강한 미생물응집체인 슬러지를 수거폐기하기 위한 종래의 슬러지외부배출라인에 슬러지를 정화처리 제1단계인 전반응조로 내부반송시킬 수 있는 유로전환밸브와 슬러지내부반송파이프라인을 추가설치하여 슬러지의 반복활용에 의한 하,폐수처리성능의 향상을 기할 수 있는 슬러지의 내부반송장치를 제공하기 위한 것이다.The present invention is a flow path switching valve capable of returning the sludge to the pre-reactor, which is the first step of the purification process to clean the sewage in the conventional main reaction tank and to collect and dispose of the sludge, which is a settled microorganism aggregate. And it is to provide a sludge internal conveying device that can further improve the performance of sewage and waste water treatment by the additional sludge internal conveying pipeline.

또한, 국내의 일반적인 하,폐수 처리장의 생물학적 반응조의 부유고형물중 무기부유고형물은 60%이상인 경우가 많아서 무기부유고형물의 비율이 상당히 높은 편이고, 본 발명과 같이 정화된 처리수의 유출량 및 유출시간을 간헐적으로 시행하되 그러한 간헐적인 유출과정을 주기적으로 시행하면서 생물학적반응기간이 장기간적인 간헐주기장기폭기식 하,폐수처리장치에서는 생물학적 하,폐수처리의 중요한 인자인 용존산소유지문제는 공기공급밸브로부터의 공기공급시간을 1회 폭기시 0∼24분까지 조절하여 적정용존산소농도를 유지토록 설계되어 있으나 적정용존산소농도(3∼6mg/l)를 유지하기 위하여 공기공급밸브에 의한 공기공급시간을 짧게하면 미생물이 급격히 침전하므로 하수와 미생물의 접촉시간이 짧아서 유기물처리효율이 저하되는 단점이 있었으므로 반응공정내의 미생물과 하수중의 유기물이 접촉할 수 있는 충분한 조건을 형성시켜 주어야 만족할만한 처리효과를 기대할 수 있었다.In addition, the inorganic solids of the suspended solids in the biological reaction tank of the general sewage, wastewater treatment plant in Korea is often 60% or more, so the ratio of inorganic solids is quite high, and the flow rate and outflow time of the purified water as in the present invention The intermittent run-off process is performed intermittently, but in the intermittent long-term aeration system of long-term intermittent aeration and wastewater treatment system, the problem of dissolved oxygen maintenance, which is an important factor of biological wastewater treatment, comes from the air supply valve. It is designed to maintain the proper dissolved oxygen concentration by adjusting the air supply time to 0 ~ 24 minutes in one aeration, but to shorten the air supply time by the air supply valve to maintain the proper dissolved oxygen concentration (3 ~ 6mg / l). When the microorganisms settle rapidly, the contact time between sewage and microorganisms is short, which reduces the efficiency of organic matter treatment. Since there was need to form a sufficient condition that the organic matter in the wastewater and the microorganisms in the reaction process can contact could expect a satisfactory treatment effect.

이러한 조건을 형성시켜주기 위하여 종래의 간헐주기장기폭기식 하,폐수처리장치에서 슬러지의 상기와 같은 내부반송파이프라인을 추가로 설치하여 전반응조에서 하,폐수중의 많은 유기물이 슬러지의 미생물과 접촉하도록 하므로서 미생물의 활성을 도모하여 하,폐수처리효율을 높이고자 함에 있다.In order to form these conditions, in the conventional intermittent long-term aeration type, additional internal conveying pipelines of sludge are installed in the wastewater treatment apparatus, and many organic substances in the wastewater and wastewater in the pre-reactor are contacted with the microorganisms of the sludge. By promoting the activity of microorganisms to improve the wastewater treatment efficiency.

도1은 본 발명의 일부단면한 사시도1 is a partial cross-sectional perspective view of the present invention

도2는 본 발명의 측단면도Figure 2 is a side cross-sectional view of the present invention.

<도면의 주요부분에 대한 부호설명><Code Description of Main Parts of Drawing>

1:유입구1: inlet

2:주반응조2: main reactor

3:격벽3: bulkhead

4:전반응조4: pre-reactor

5:공기공급밸브5: air supply valve

6:유통구6: distribution outlet

7:디캔터7: Decanter

8:배출구8: outlet

9:배출관9: exhaust pipe

10:당김봉10: pull Kimbong

11:오버플로우턱11: overflow jaw

12:슬러지펌프12: sludge pump

13:슬러지외부배출파이프라인13: Sludge outflow pipeline

14:슬러지내부반송파이프라인14: Sludge Internal Transfer Pipeline

15:유로전환밸브15: flow path switching valve

이하 본 발명의 바람직한 실시예를 첨부도면에 따라 상세히 설명하면 다음과 같다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도1 내지 도2에서와 같이 도시하수및 산업폐수등의 하,폐수가 유입구(1)로 유입되어 주반응조(2)와 격벽(3)으로 막혀진 전반응조(4)에서 별도의 송풍기에 의한 공기공급밸브(5)로부터 공급되는 공기와 혼합되면 미생물의 활성에 의하여 유기오탁물이 분해되면서 침전되어 격벽(3)하부의 유통구(6)를 통하여 주반응조(2)로 유입된다.As shown in FIGS. 1 and 2, separate wastewater is discharged from the pre-reactor 4, in which the sewage and wastewater, such as urban sewage and industrial wastewater, are introduced into the inlet 1 and blocked by the main reactor 2 and the partition 3. When mixed with the air supplied from the air supply valve (5), the organic soil is decomposed by the activity of the microorganisms are precipitated and introduced into the main reaction tank (2) through the outlet (6) below the partition (3).

주반응조(2)에 유입된 하,폐수가 또다시 바닥의 공기공급밸브(5)로부터 공급되는 공기로 폭기혼합되면 하,폐수중의 여러가지 호기성 미생물이 유기오탁물을 분해, 산화하고 생물학적산화, 질산화, 탈질, 탈인 및 고액분리가 이루어져 깨끗한 상등수는 상부에 형성되고, 고형물은 하부에 침전되는 것으로서 상부의 깨끗한 상등수는 상등수유출장치인 디캔터(Decanter)(7)에 의하여 배출구(8)를 통하여 강이나 바다로 흘러나가게 되는 것이다.When the wastewater and wastewater introduced into the main reaction tank 2 are aeration mixed with the air supplied from the air supply valve 5 at the bottom, various aerobic microorganisms in the wastewater and wastewater decompose and oxidize the organic soil, By nitrification, denitrification, dephosphorization, and solid-liquid separation, the clean supernatant is formed at the top, and the solid is precipitated at the bottom. The clean supernatant at the top is formed through the outlet (8) by a decanter (7), a supernatant outlet. It will flow out to the sea.

여기서 디캔터(Decanter)(7)는 공지된 처리수 유출장치이나 그 구성을 간단히 설명하면 배출구(8)와 연동되고 있는 배출관(9)을 축으로 하여 디캔터(Decanter)(7)가 당김봉(10)의 당기고 미는 작동으로 회전되어 수면과 수평위치에 위치된 디캔터(Decanter)(7)의 오버플로우턱(11)으로 깨긋한 처리수가 넘쳐흘러 들어가서 배출관(9)및 배출구(8)를 통하여 강이나 바다로 흘러나가게 된다.Here, the decanter 7 is a known treatment water outlet device or a brief description of the configuration thereof, and the decanter 7 pulls the rod 10 around the discharge pipe 9 interlocked with the outlet 8. Rotation is pulled and pushed to the overflow jaw (11) of the decanter (7) located in the water and horizontal position overflows the treated water flow through the discharge pipe (9) and outlet (8) It flows out to sea.

또한, 미생물의 공기에 의한 활성증식으로 하수의 정화처리를 하면서 미생물이 유기,무기의 부유고형물과 응집하여 침강된 활성슬러지중 슬러지는 슬러지펌프(12)에 의하여 펌핑수거되어 슬러지외부배출파이프라인(13)을 통하여 외부로 배출 폐기되도록 구성되어 있으나,In addition, the sludge in the activated sludge, which is precipitated by the microorganism agglomerated with organic and inorganic suspended solids, is collected and pumped by the sludge pump 12 while purifying the sewage by the active growth by the air of the microorganisms. 13) is configured to be discharged to the outside through the disposal,

이러한 슬러지외부배출파이프라인(13)의 중간에 본 발명에 있어서 가장 중요한 구성인 슬러지의 전반응조(4)로의 내부반송을 위한 슬러지내부반송파이프라인(14)이 3방밸브인 유로전환밸브(15)를 분기점으로 하여 연결되도록 구성하고, 유로전환밸브(15)의 유로가 전반응조(4)로 개통되도록 밸브조작을하여 슬러지외부배출파이프라인(13)을 폐쇄시켜 전반응조(4)로 반송시키도록하고, 슬러지의 외부배출폐기가 필요하면 유로전환밸브(15)의 유로가 슬러지 외부배출파이프라인(13)과 개통되도록 밸브조작을 하여 슬러지의 일부만 외부배출되어 폐기되도록 하므로서 미생물이 들어있는 슬러지의 전반응조(4)로의 반복반송에 의한 재활용으로 미생물과 하수유기물의 접촉을 증대하여 하,폐수처리의 효율성을 제고시킨 것이다.In the middle of the sludge external discharge pipeline 13, the sludge inner conveying pipeline 14 for the internal conveyance of the sludge to the pre-reaction tank 4, which is the most important configuration in the present invention, is a three-way valve. ) Is connected to the pre-reactor (4) by closing the sludge external discharge pipe line (13) by operating the valve so that the flow path of the flow path switching valve (15) is opened to the pre-reactor (4). If the external discharge waste of sludge is needed, the valve is operated so that the flow path of the flow path switching valve 15 is opened with the sludge external discharge pipeline 13 so that only a part of the sludge is discharged externally and discarded. Recycling by repeated transport to the pre-reactor 4 increases the efficiency of wastewater and wastewater treatment by increasing the contact of microorganisms and sewage organics.

간헐주기장기폭기식 하,폐수처리장치의 주반응조(2)에서 외부로 배출폐기 하였던 슬러지의 전반응조(4)로의 내부반송을 실시하므로서 슬러지의 각종미생물이 하수의 유기물과의 접촉시간이 증가되어 유기물,질소 및 인의 제거 효율을 향상시키므로 하,폐수처리의 효율성을 향상시킨 발명이다.Under the intermittent long-term aeration type, the internal transport of the sludge from the main reaction tank (2) of the wastewater treatment system to the pre-reactor (4) was discharged to the outside, so that various microorganisms of the sludge increased contact time with organic matter in the sewage. It is an invention that improves the efficiency of sewage and wastewater treatment because it improves the removal efficiency of organic matter, nitrogen and phosphorus.

Claims (1)

하,폐수를 전반응조(4)및 주반응조(2)에서 공기공급밸브(5)에 의한 공기로 폭기 혼합하여 미생물의 유기물분해에 의하여 정화처리하는 하,폐수처리장치에 있어서,In the wastewater treatment apparatus, the wastewater is aerated by mixing the wastewater with air by the air supply valve (5) in the pre-reactor (4) and the main reactor (2) and purified by organic decomposition of microorganisms. 주반응조(2)의 슬러지를 슬러지펌프(12),유로전환밸브(15) 및 슬러지내부반송파이프라인(14)을 통하여 전반응조(4)로 내부반송시켜 슬러지의 미생물의 반복반송에 의한 재활용으로 하,폐수처리의 성능을 향상시킨 내부반송형 간헐주기장기폭기식 하,폐수처리장치.The sludge of the main reaction tank (2) is conveyed internally to the pre-reactor (4) through the sludge pump (12), the flow path switching valve (15), and the sludge inner conveying pipeline (14), and the sludge is recycled by the repeated transport of microorganisms. Internal transport type intermittent long-term aeration type sewage and wastewater treatment system with improved performance of sewage and wastewater treatment.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5013441A (en) * 1988-07-20 1991-05-07 Goronszy Mervyn C Biological nutrient removal with sludge bulking control in a batch activated sludge system
JPH04354595A (en) * 1991-05-30 1992-12-08 Kubota Corp Sewage treating equipment
JPH09150181A (en) * 1995-12-01 1997-06-10 Nishihara Environ Sanit Res Corp Sewage purifying device
KR20020091723A (en) * 2001-05-31 2002-12-06 아태수기엔지니어링 주식회사 Waste water disposal method by continuos inflow Sequencing Bath Reactor and its apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5013441A (en) * 1988-07-20 1991-05-07 Goronszy Mervyn C Biological nutrient removal with sludge bulking control in a batch activated sludge system
JPH04354595A (en) * 1991-05-30 1992-12-08 Kubota Corp Sewage treating equipment
JPH09150181A (en) * 1995-12-01 1997-06-10 Nishihara Environ Sanit Res Corp Sewage purifying device
KR20020091723A (en) * 2001-05-31 2002-12-06 아태수기엔지니어링 주식회사 Waste water disposal method by continuos inflow Sequencing Bath Reactor and its apparatus

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