KR100628881B1 - Intensive Wastewater Treatment System - Google Patents

Intensive Wastewater Treatment System Download PDF

Info

Publication number
KR100628881B1
KR100628881B1 KR1020050059998A KR20050059998A KR100628881B1 KR 100628881 B1 KR100628881 B1 KR 100628881B1 KR 1020050059998 A KR1020050059998 A KR 1020050059998A KR 20050059998 A KR20050059998 A KR 20050059998A KR 100628881 B1 KR100628881 B1 KR 100628881B1
Authority
KR
South Korea
Prior art keywords
tank
sludge
water
wastewater
wastewater treatment
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.)
Expired - Lifetime
Application number
KR1020050059998A
Other languages
Korean (ko)
Other versions
KR20060071838A (en
Inventor
진성언
Original Assignee
진성언
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 진성언 filed Critical 진성언
Priority to KR1020050059998A priority Critical patent/KR100628881B1/en
Publication of KR20060071838A publication Critical patent/KR20060071838A/en
Application granted granted Critical
Publication of KR100628881B1 publication Critical patent/KR100628881B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0012—Settling tanks making use of filters, e.g. by floating layers of particulate material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0048—Plurality of plates inclined in alternating directions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2444—Discharge mechanisms for the classified liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/245—Discharge mechanisms for the sediments
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5227—Processes for facilitating the dissolution of solid flocculants in water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/002—Construction details of the apparatus

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Clinical Laboratory Science (AREA)
  • Inorganic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

소량의 폐수를 배출하는 기업체나 업소에서 저렴한 설치비용으로 설치함은 물론이고 좁은 공간에서도 설치가 용이하고 저렴한 비용으로 도모하여 정화효과를 높일수 있도록 개별적으로 구성된 여러단계의 폐수정화처리장치를 하나의 폐수처리장치에 집약적으로 형성한 폐수처리장치를 제공하는 것이다.In addition to the low cost of installation in companies and businesses that discharge a small amount of wastewater, it is easy to install in a narrow space and promotes the purification efficiency at a low cost. It is to provide a wastewater treatment apparatus intensively formed in the treatment apparatus.

이와같은 목적을 달성하기 위하여 본 발명은 최초 폐수를 저장하는 폐수집수조와 펌프 및 폐수공급파이프를 통하여 상기 폐수집수조에서 유입된 폐수가 반응조 및 응집조에서 반응제 및 응집제의 투입으로 인해 슬러지의 응집을 발생시켜 침전조를 통해 침전방식으로 슬러지를 분리시키고 폐수는 필터방식으로 정화처리되어 배출되는 것으로 구성된 일체형의 폐수처리장치를 제공한다.In order to achieve the above object, the present invention provides the sludge agglomeration due to the addition of the reactant and the flocculant into the reaction tank and the flocculation tank through the waste water collection tank, the pump and the waste water supply pipe storing the initial waste water. It is produced by the sedimentation through the sedimentation tank to separate the sludge, and the waste water is provided by the filter method of the integrated wastewater treatment device consisting of the discharged.

또한, 침전조에서 슬러지의 침전과 분리를 극대화하기 위해 침전조로 유입되는 폐수의 유량의 흐름을 조절시키는 갈매기형상의 갈매기형 바플(baffle)을 설치하여 폐수가 침전조 내부로 자유낙하 대신 안정적인 낙하를 유도하는 갈매기형 바플을 설치하여 폐수와 슬러지의 상분리효율을 극대화하기 위함이다.In addition, in order to maximize the sedimentation and separation of sludge in the sedimentation tank, a seagull-shaped gull baffle is installed to control the flow of wastewater flowing into the sedimentation tank to induce a stable fall instead of free fall into the sedimentation tank. This is to maximize the phase separation efficiency of wastewater and sludge by installing chevron baffles.

Description

집약적 폐수처리장치{Compact waste water treatment apparatus}Intensive waste water treatment apparatus

도 1은 본 발명에 따른 집약적 폐수처리장치의 폐수처리공정을 나타낸 공정도1 is a process chart showing the wastewater treatment process of the intensive wastewater treatment apparatus according to the present invention

도 2는 본 발명에 따른 집약적 폐수처리장치의 폐수처리공정을 나타낸 구성도2 is a block diagram showing a wastewater treatment process of the intensive wastewater treatment apparatus according to the present invention

도 3은 본 발명에 따른 집약적 폐수처리장치중에 침전조를 나타낸 사시도Figure 3 is a perspective view showing a sedimentation tank in the intensive wastewater treatment apparatus according to the present invention

도 4는 본 발명에 따른 집약적 폐수처리장치중에 침전조의 내부단면사시도Figure 4 is an internal cross-sectional perspective view of the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention

도 5는 본 발명에 따른 집약적 폐수처리장치중에 침전조 내부에 처리수와 슬러지가 분리되는 것을 나타낸 개념단면도5 is a conceptual cross-sectional view showing that the treated water and sludge is separated inside the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention.

도 6은 본 발명에 따른 집약적 폐수처리장치에서 침전조에 구비된 갈매기형 바플(baffle)의 확대사시도6 is an enlarged perspective view of a chevron baffle provided in the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention;

도 7은 본 발명에 따른 집약적 폐수처리장치에서 침전조에 구비된 타공차단막의 확대사시도Figure 7 is an enlarged perspective view of the perforated barrier membrane provided in the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention

도 8은 본 발명에 따른 집약적 폐수처리장치에서 폐수처리시설물이 집약된 케비넷형상의 하우징의 사시도8 is a perspective view of a cabinet-shaped housing in which wastewater treatment facilities are concentrated in the intensive wastewater treatment apparatus according to the present invention;

〈도면의 주요부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>

집약적 폐수처리장치 : 100 제2배출관 : 430Intensive wastewater treatment system: 100 Secondary discharge pipe: 430

집수조 : 200 갈매기형 바플(baffle) : 440Sump: 200 gull baffle: 440

원수펌프 : 210 수직면 : 440aRaw water pump: 210 Vertical surface: 440a

원수공급관 : 220 예각면 : 440bRaw water supply pipe: 220 Acute angle: 440b

반응응집조 : 300 둔각면 : 440cReaction coagulation tank: 300 obtuse surface: 440c

교반기 : 310 타공차단막 : 500Stirrer: 310 Perforated Blocker: 500

블러워 : 320 타공 : 510Blur: 320 Perforation: 510

PH제어기 : 330 톱니 : 520PH controller: 330 teeth: 520

공기공급라인 : 340 슬러지저장탱크 : 600Air Supply Line: 340 Sludge Storage Tank: 600

반응제공급탱크 : 350 탈수기 : 650Reagent Supply Tank: 350 Dehydrator: 650

응집제공급탱크 : 360 슬러지배출관 : 660Coagulant supply tank: 360 Sludge discharge pipe: 660

정량펌프 : 370 모래여과조 : 700Metering pump: 370 Sand filtration tank: 700

침전조 : 400 활성탄여과조 : 800Sedimentation tank: 400 Activated carbon filtration tank: 800

혼합수공급관 : 410 방류관 : 810Mixed Water Supply Pipe: 410 Discharge Pipe: 810

제1배출관 : 420 하우징 : 900First discharge pipe: 420 Housing: 900

일반적으로 산업시설을 이용하여 각종 제품등을 생산하는데 있어 필히 생산제품을 제조하는 재료의 세척, 도금, 냉각, 도색, 피막, 유리가공 등의 작업과정을 거쳐 최종적으로 제조되는 필요한 제품들이 만들어 지게 되며, 이러한 과정을 거치 는 동안에 여러가지 오염물이 뒤섞인 폐수가 발생이 된다.In general, in the production of various products using industrial facilities, the necessary products are finally manufactured through the process of washing, plating, cooling, painting, coating, and glass processing. In the course of this process, wastewater mixed with various contaminants is generated.

일반적으로 폐수란 유기물 및 무기물이 혼입되어 그대로 사용할 수 없는 물을 일컫는 것으로 산업화로 인한 각종 설비나 제조과정에서 폐수가 발생되고 있다.In general, wastewater refers to water that is mixed with organic and inorganic materials and cannot be used as it is. Wastewater is generated in various facilities and manufacturing processes due to industrialization.

이때, 발생되는 폐수는 통상 자연이 자연 정화할 수 있는 한계를 넘고, 또한 그 폐수량이 상대적으로 많고 이를 무단방류를 하게 되면 하천과 강 및 바다로 흘러들어 이 모두를 오염시키게 된다.At this time, the wastewater generated is usually beyond the limit that can be naturally purified by nature, and also the amount of the wastewater is relatively large, and if it is endlessly discharged, it flows into rivers, rivers, and the sea to contaminate all of them.

이를 방지하기 위해 폐수는 일정수준으로 정화시킨 상태에서 방출하도록 되어 있으며, 폐수 정화를 위한 각종 장치와 화학처리제 또는 생물학 처리제가 사용되어지고 있다.In order to prevent this, the waste water is discharged in a state of being purified to a certain level, and various apparatuses and chemical or biological treatment agents are used for the purification of waste water.

일반적으로 사용되는 폐수처리시설에 각종 장치를 사용하여 폐수를 정화하게 되면 정화된 폐수중에 부유되어 있는 응집된 슬러지를 침전하는데 많은 시간이 소비되는 등 그 효율이 저하되어 응집제를 투여한 후 침전을 유도하기 위한 반응조, 응집조, 침전조, 여과조의 4가지 이상의 대단위 폐수저장조를 갖추어 폐수를 정화시키는 시설을 준비하고 있다. 처리조로 모인 폐수를 펌프를 이용하여 상부에 있는 여과조로 보내져 분리되며 이때 여과를 가속화하기 위해 여과조 내의 압력을 일정압력으로 가압을 한다.When the wastewater is purified by using various devices in the commonly used wastewater treatment facilities, the efficiency is reduced, as it takes a lot of time to settle the flocculated sludge suspended in the purified wastewater. We have four or more large-scale wastewater storage tanks, such as a reaction tank, a flocculation tank, a precipitation tank, and a filtration tank, to prepare wastewater purification facilities. The wastewater collected in the treatment tank is sent to a filtration tank at the top using a pump and separated. At this time, the pressure in the filtration tank is pressurized to a constant pressure to accelerate the filtration.

이러한 과정을 거친 슬러지들은 분류도관에 축척이 되고 배출구에 매달린 여과포에 의해 걸러지게 되며 이때 여과포에 의해 걸러지게 되는 슬러지를 강하게 뭉쳐서 외부로 배출하여 폐수를 정화하는 것이나 여과포를 통과하면서 정화된 물이 하부로 자연 낙하되어 주위로 되게 되는 문제점이 있었다.The sludge that has undergone this process is accumulated by the filter cloth suspended in the sorting conduit and suspended by the filter cloth. At this time, the sludge that is filtered by the filter cloth is strongly packed together and discharged to the outside to purify the wastewater or the purified water is passed through the filter cloth. There was a problem that the natural fall into the surroundings.

그리고 여과포에 채워진 슬러지 등을 수시로 교체를 해주어야 되는 번거로움이 있었다.And there was a hassle to replace the sludge and the like filled in the filter cloth from time to time.

또한 종래 사용되는 대부분의 폐수처리장치는 장치설비에 많은 비용이 소요되고 있으며 또한 대규모적인 공간을 차지하기 때문에 소규모 사업단지와 같은 기업체에서는 오염도가 심한 소규모사업장에서 설치하는데 많은 어려움이 있었다. 특히 소규모 기업체등의 발생되는 폐수는 오염도가 높은 농축된 체로 그대로 방출되는 경우가 많기 때문에 이것을 처리하는데 많은 비용이 소요되고 폐수를 정화하기 위해 대규모적인 공간을 차지하는 등 폐수처리에 대한 환경적인 문제로 대두되고 있다.In addition, since most of the conventional wastewater treatment devices are expensive to install equipment and occupy a large amount of space, there are many difficulties in installing small contaminated workplaces in enterprises such as small business complexes. In particular, wastewater generated by small companies is often discharged as concentrated pollutants with high pollution. Therefore, it is expensive to treat this, and it takes up a large amount of space to purify the wastewater. It is becoming.

상기 종래의 대규모 폐수처리장치에는 배출되는 폐수를 저장하는 집수조가 있으며, 상기 집수조에 모인 폐수를 일정량으로 연속적으로 공급받아 유기 및 무기물질 등의 반응제 및 응집제로 폐수에 함유된 슬러지로 침전시켜 분리되는 반응조와 응집조가 있으며, 상기 폐수와 침전된 슬러지로 분리시키는 침전조로 구성되는 연속식의 폐수처리장치를 구비하고 있다.The conventional large-scale wastewater treatment apparatus has a collecting tank for storing the discharged wastewater, and the wastewater collected in the collecting tank is continuously supplied in a predetermined amount and precipitated and separated into sludge contained in the wastewater as a reactant and flocculant such as organic and inorganic substances. There are a reaction tank and an agglomeration tank, and a continuous wastewater treatment apparatus composed of a sedimentation tank separating the wastewater and the precipitated sludge is provided.

상기와 같은 대규모 폐수처리장치에서 규모가 큰 집수조, 반응조, 응집조, 침전조, 여과조 등으로 구성하고 있으며, 상기 폐수처리시설을 설치되는 공간에 제약을 받고 있으며, 설비비용이 고가인점이 문제점으로 대두되고 있다.In the large-scale wastewater treatment system as described above, it consists of a large collection tank, a reaction tank, a flocculation tank, a sedimentation tank, a filtration tank, etc., and is constrained by the space where the wastewater treatment facility is installed. It is becoming.

또한, 폐수처리장치에서 침전조에 유입되는 폐수와 슬러지가 자유낙하식의 일정 유량으로 침전조로 흘러들어와 침전조내부에 폐수와 슬러지가 분리되지 않고 혼합된 상태로 있어 정상적인 분리가 어려우며 침전조의 폐수배출구에 응집된 슬러 지가 그대로 흘러 침전조에서 실질적인 폐수와 슬러지의 분리가 일어나지 않고 있는 실정이다.In addition, the wastewater and sludge flowing into the sedimentation tank from the wastewater treatment device flows into the sedimentation tank at a constant flow rate of free fall type, and the wastewater and the sludge are not separated and mixed inside the sedimentation tank. The sludge flows as it is, and there is no actual separation of wastewater and sludge in the sedimentation tank.

상기와 같은 이유로 인해 그대로 폐수속에 함유된 슬러지가 일반하천에 유입되어 치명적이고 높은 환경적인 문제점을 일으키고 있다.Due to the above reasons, sludge contained in the wastewater as it flows into the general river is causing fatal and high environmental problems.

본 발명은 이와같은 문제점을 감안하여 안출된 것으로써, 소량의 폐수를 배출하는 기업체나 업소에서 저렴한 설치비용으로 설치함은 물론이고 좁은 공간에서도 설치가 용이하고 저렴한 비용으로 도모하여 정화효과를 높일수 있도록 개별적으로 구성된 여러단계의 폐수정화처리장치를 하나의 폐수처리장치에 집약적으로 형성한 폐수처리장치를 제공하는 것이다.The present invention has been devised in view of such a problem, so that it can be installed at a low installation cost in a company or a business that discharges a small amount of wastewater, as well as easy to install in a narrow space, and at a low cost to enhance the purification effect It is to provide a wastewater treatment apparatus in which the wastewater purification apparatuses of several stages configured individually are intensively formed in one wastewater treatment apparatus.

이와같은 목적을 달성하기 위하여 본 발명은 최초 폐수를 저장하는 폐수집수조와 펌프 및 폐수공급파이프를 통하여 상기 폐수집수조에서 유입된 폐수가 반응조 및 응집조에서 반응제 및 응집제의 투입으로 인해 슬러지의 응집을 발생시켜 침전조를 통해 침전방식으로 슬러지를 분리시키고 폐수는 필터방식으로 정화처리되어 배출되는 것으로 구성된 일체형의 폐수처리장치를 제공한다.In order to achieve the above object, the present invention provides the sludge agglomeration due to the addition of the reactant and the flocculant into the reaction tank and the flocculation tank through the waste water collection tank, the pump and the waste water supply pipe storing the initial waste water. It is produced by the sedimentation through the sedimentation tank to separate the sludge, and the waste water is provided by the filter method of the integrated wastewater treatment device consisting of the discharged.

또한, 침전조에서 슬러지의 침전과 분리를 극대화하기 위해 침전조로 유입되는 폐수의 유량의 흐름을 조절시키는 갈매기형상의 갈매기형 바플(baffle)을 설치하여 폐수가 침전조 내부로 자유낙하 대신 안정적인 낙하를 유도하는 갈매기형 바플을 설치하여 폐수와 슬러지의 상분리효율을 극대화하기 위해 본 발명의 폐수처리장치를 제공하는데 그 목적으로 하고 있다.In addition, in order to maximize the sedimentation and separation of sludge in the sedimentation tank, a seagull-shaped gull baffle is installed to control the flow of wastewater flowing into the sedimentation tank to induce a stable fall instead of free fall into the sedimentation tank. It is an object of the present invention to provide a wastewater treatment apparatus of the present invention in order to maximize the phase separation efficiency of wastewater and sludge by installing a chevron baffle.

상기 목적을 달성하기 위한 본 발명의 폐수처리장치는 캐비넷형상을 가지고 있는 하우징(900)내부에 폐수처리시설이 집약적인 구비되는 집약적 폐수처리장치(100)에 있어서,In the wastewater treatment apparatus of the present invention for achieving the above object in the intensive wastewater treatment apparatus 100 is provided with a intensive wastewater treatment facility in the housing 900 having a cabinet shape,

폐수의 원수를 저장하는 집수조(200)와,A water collecting tank 200 for storing raw water of wastewater,

상기 집수조(200)에서 원수펌프(210)가 설치된 원수공급관(220)을 통해 폐수를 공급받는 반응응집조(300)와,A reaction agglomeration tank 300 for receiving wastewater through a raw water supply pipe 220 in which a raw water pump 210 is installed in the water collecting tank 200;

상기 반응응집조(300)에 공급된 폐수를 처리수와 슬러지의 분리 및 응집을 위해 혼합되는 반응제와 응집제는 각각 정량펌프(370)가 설치된 반응제공급탱크(350)와 응집제공급탱크(360)에 의해 반응응집조(300)에 유입되고 폐수와의 고른 혼합을 위해 반응응집조(300)에 구비된 교반기(310)에 의해 혼합되고,The reactant and flocculant mixed with the wastewater supplied to the reaction agglomeration tank 300 for the separation and flocculation of the treated water and sludge, respectively, the reactant supply tank 350 and the flocculant supply tank 360 in which the metering pump 370 is installed. Into the reaction agglomeration tank 300 by a) and mixed by the stirrer 310 provided in the reaction agglomeration tank 300 for even mixing with the waste water,

상기 반응응집조(300)에서 처리수와 슬러지로 혼합된 혼합수가 처리수와 슬러지로 분리 및 침전되기 위해 상부의 일측에 혼합수를 공급받는 혼합수공급관(410)과 상부의 다른일측에는 처리수가 배출되는 제1배출관(420)이 있으며 하부의 일측에는 슬러지를 배출하는 제2배출관(430)이 연결되어 있는 침전조(400)와,In the reaction agglomeration tank 300, the mixed water mixed with the treated water and sludge is treated water and the mixed water supply pipe 410 receiving the mixed water on one side of the upper part in order to separate and settle the treated water and sludge. There is a first discharge pipe 420 is discharged and the settling tank 400 is connected to the second discharge pipe 430 for discharging the sludge on one side of the lower,

상기 침전조(400)의 내부 공간에는 혼합수가 혼합수공급관(410)을 통해 유입되는 유량의 흐름을 조절하여 더욱 안정적으로 혼합수가 낙하하도록 하는 수직방향으로 다수 구획하며 양측면이 침전조(400)의 내부양측면에 용접에 의해 접합되어 구비된 갈매기형상의 갈매기형 바플(baffle)(440)과,The inner space of the settling tank 400 is divided into a plurality of vertical direction to allow the mixed water to fall more stably by controlling the flow of the flow rate of the mixed water flowing through the mixed water supply pipe 410, both sides of the inner both sides of the settling tank 400 Chevron-shaped chevron baffles 440 which are joined to each other by welding,

상기 갈매기형 바플(baffle)(440)의 상·하부에 일정길이만큼 수직면(440a) 을 가지고 있으며 상·하부사이에는 일정길이의 예각면(440b)과 예각면(440b)과 같은 길이의 둔각면(440c)이 ">"형상으로 연결되어 구비되고,The upper and lower portions of the chevron baffle 440 has a vertical surface 440a by a predetermined length, and the upper and lower obtuse surfaces having the same length as the acute angle 440b and the acute angle 440b. 440c is provided connected in a ">" shape,

상기 침전조(400)에 처리수가 배출되는 제1배출관(420)이 연결되어 있는 공간주위에 "└"형태로 제1배출관(420) 연결주위에 용접처리되어 부착되며 전체적인 형상이 1-8mm의 타공(510)으로 이루어진 판상결합체며 상단부는 톱니(520)가 형성되어 있으며 처리수에 함유된 미처리된 슬러지와 부유물을 처리하기 위한 타공차단막(500)과,Welded around the first discharge pipe 420 connection in the form of "└" around the space where the first discharge pipe 420 is discharged to the sedimentation tank 400 is connected, the overall shape is 1-8mm perforated A plate-shaped assembly having an upper portion 510 is formed with a tooth 520, and a perforated barrier membrane 500 for treating untreated sludge and suspended matter contained in the treated water,

상기 침전조(400)에서 제2배출관(430)을 통해 흘러나온 슬러지를 저장하는 슬러지저장탱크(600)와,Sludge storage tank 600 for storing the sludge flowed out through the second discharge pipe 430 in the settling tank 400,

상기 슬러지저장탱크(600)에서 저장된 슬러지를 탈수하기 위해 탈수기(650)를 거쳐 최종슬러지를 배출하는 슬러지배출관(660)가 구비되고,Sludge discharge pipe 660 is provided to discharge the final sludge through the dehydrator 650 to dewater the sludge stored in the sludge storage tank 600,

상기 침전조(400)에서 배출되는 처리수는 유량계가 연결된 배출관을 통해 일정량을 1차적으로 필터작용을 하는 모래가 구비된 모래여과조(700)에 의해 여과되고,The treated water discharged from the settling tank 400 is filtered by a sand filtration tank 700 provided with sand that primarily filters a predetermined amount through a discharge pipe to which a flowmeter is connected.

상기 모래여과조(700)를 거친 처리수는 2차적인 필터작용을 위해 활성탄이 구비된 활성탄여과조(800)에 의해 여과되어 방류관(810)을 통해 방류수가 배출되는 것을 구비되어 캐비넷형상의 하우징(900)내부에 상기 모든 구조물이 집약적으로 구비되는 집약적 폐수처리장치(100)에 관한 것이다.The treated water having passed through the sand filtration tank 700 is filtered by an activated carbon filtration tank 800 equipped with activated carbon for a secondary filter action, and discharged water is discharged through the discharge pipe 810. 900 refers to an intensive wastewater treatment apparatus 100 in which all the structures are intensively provided therein.

본 발명의 상기의 목적을 달성하기 위하여 이하의 구체적인 기술내용을 첨부도면에 의거하여 자세히 설명하면 다음과 같다.In order to achieve the above object of the present invention will be described in detail based on the accompanying technical details as follows.

도 1은 본 발명에 따른 집약적 폐수처리장치의 폐수처리공정을 나타낸 공정도이고,1 is a process chart showing a wastewater treatment process of the intensive wastewater treatment apparatus according to the present invention,

도 2는 본 발명에 따른 집약적 폐수처리장치의 폐수처리공정을 나타낸 구성도이고,2 is a block diagram showing a wastewater treatment process of the intensive wastewater treatment apparatus according to the present invention,

도 3은 본 발명에 따른 집약적 폐수처리장치중에 침전조를 나타낸 사시도이고,3 is a perspective view showing a sedimentation tank in the intensive wastewater treatment apparatus according to the present invention,

도 4는 본 발명에 따른 집약적 폐수처리장치중에 침전조의 내부단면사시도이고,Figure 4 is an internal cross-sectional perspective view of the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention,

도 5는 본 발명에 따른 집약적 페수처리장치중에 침전조 내부에 처리수와 슬러지가 분리되는 것을 나타낸 개념단면도이고,5 is a conceptual cross-sectional view showing that the treated water and the sludge is separated inside the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention,

도 6은 본 발명에 따른 집약적 폐수처리장치에서 침전조에 구비된 갈매기형 바플(baffle)의 확대사시도이고,6 is an enlarged perspective view of a gull baffle provided in the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention,

도 7은 본 발명에 따른 집약적 폐수처리장치에서 침전조에 구비된 타공차단막의 확대사시도이고,Figure 7 is an enlarged perspective view of the perforated barrier membrane provided in the sedimentation tank in the intensive wastewater treatment apparatus according to the present invention,

도 8은 본 발명에 따른 집약적 폐수처리장치에서 폐수처리시설물이 집약된 캐비넷형상의 하우징의 사시도이다.8 is a perspective view of a cabinet-shaped housing in which wastewater treatment facilities are concentrated in the intensive wastewater treatment apparatus according to the present invention.

본 발명의 구성은 도 2의 폐수처리공정의 구성도에 나타낸 바와 같이 캐비넷형상을 가지고 있는 하우징(900)내부에 폐수처리시설이 집약적인 구비되는 집약적 폐수처리장치(100)에 있어서,In the constitution of the present invention, in the intensive wastewater treatment apparatus 100 in which the wastewater treatment facility is intensively provided in the housing 900 having a cabinet shape as shown in the schematic diagram of the wastewater treatment process of FIG.

폐수의 원수를 저장하는 집수조(200)와,A water collecting tank 200 for storing raw water of wastewater,

상기 집수조(200)에서 원수펌프(210)가 설치된 원수공급관(220)을 통해 폐수를 공급받는 반응응집조(300)와,A reaction agglomeration tank 300 for receiving wastewater through a raw water supply pipe 220 in which a raw water pump 210 is installed in the water collecting tank 200;

상기 반응응집조(300)에 공급된 폐수를 처리수와 슬러지의 분리 및 응집을 위해 혼합되는 반응제와 응집제는 각각 정량펌프(370)가 설치된 반응제공급탱크(350)와 응집제공급탱크(360)에 의해 반응응집조(300)에 유입되고 폐수와의 고른 혼합을 위해 반응응집조(300)에 구비된 교반기(310)에 의해 혼합되고,The reactant and flocculant mixed with the wastewater supplied to the reaction agglomeration tank 300 for the separation and flocculation of the treated water and sludge, respectively, the reactant supply tank 350 and the flocculant supply tank 360 in which the metering pump 370 is installed. Into the reaction agglomeration tank 300 by a) and mixed by the stirrer 310 provided in the reaction agglomeration tank 300 for even mixing with the waste water,

상기 반응응집조(300)에서 처리수와 슬러지로 혼합된 혼합수가 처리수와 슬러지로 분리 및 침전되기 위해 상부의 일측에 혼합수를 공급받는 혼합수공급관(410)과 상부의 다른일측에는 처리수가 배출되는 제1배출관(420)이 있으며 하부의 일측에는 슬러지를 배출하는 제2배출관(430)이 연결되어 있는 침전조(400)와,In the reaction agglomeration tank 300, the mixed water mixed with the treated water and sludge is treated water and the mixed water supply pipe 410 receiving the mixed water on one side of the upper part in order to separate and settle the treated water and sludge. There is a first discharge pipe 420 is discharged and the settling tank 400 is connected to the second discharge pipe 430 for discharging the sludge on one side of the lower,

상기 침전조(400)의 내부 공간에는 혼합수가 혼합수공급관(410)을 통해 유입되는 유량의 흐름을 조절하여 더욱 안정적으로 혼합수가 낙하하도록 하는 수직방향으로 다수 구획하며 양측면이 침전조(400)의 내부양측면에 용접에 의해 접합되어 구비된 갈매기형상의 갈매기형 바플(baffle)(440)과,The inner space of the settling tank 400 is divided into a plurality of vertical direction to allow the mixed water to fall more stably by controlling the flow of the flow rate of the mixed water flowing through the mixed water supply pipe 410, both sides of the inner both sides of the settling tank 400 Chevron-shaped chevron baffles 440 which are joined to each other by welding,

상기 갈매기형 바플(baffle)(440)의 상·하부에 일정길이만큼 수직면(440a)을 가지고 있으며 상·하부사이에는 일정길이의 예각면(440b)과 예각면(440b)과 같은 길이의 둔각면(440c)이 ">"형상으로 연결되어 구비되고,The upper and lower portions of the chevron baffle 440 has a vertical surface 440a by a predetermined length, and the upper and lower obtuse surfaces having the same length as the acute angle 440b and the acute angle 440b. 440c is provided connected in a ">" shape,

상기 침전조(400)에 처리수가 배출되는 제1배출관(420)이 연결되어 있는 공간주위에 "└"형태로 제1배출관(420) 연결주위에 용접처리되어 부착되며 전체적인 형상이 1-8mm의 타공(510)으로 이루어진 판상결합체며 상단부는 톱니(520)가 형성 되어 있으며 처리수에 함유된 미처리된 슬러지와 부유물을 처리하기 위한 타공차단막(500)과,Welded around the first discharge pipe 420 connection in the form of "└" around the space where the first discharge pipe 420 is discharged to the sedimentation tank 400 is connected, the overall shape is 1-8mm perforated A plate-shaped combination body having an upper portion 510 is formed with a tooth 520 and a perforated barrier film 500 for treating untreated sludge and suspended matter contained in the treated water,

상기 침전조(400)에서 제2배출관(430)을 통해 흘러나온 슬러지를 저장하는 슬러지저장탱크(600)와,Sludge storage tank 600 for storing the sludge flowed out through the second discharge pipe 430 in the settling tank 400,

상기 슬러지저장탱크(600)에서 저장된 슬러지를 탈수하기 위해 탈수기(650)를 거쳐 최종슬러지를 배출하는 슬러지배출관(660)가 구비되고,Sludge discharge pipe 660 is provided to discharge the final sludge through the dehydrator 650 to dewater the sludge stored in the sludge storage tank 600,

상기 침전조(400)에서 배출되는 처리수는 유량계가 연결된 배출관을 통해 일정량을 1차적으로 필터작용을 하는 모래가 구비된 모래여과조(700)에 의해 여과되고,The treated water discharged from the settling tank 400 is filtered by a sand filtration tank 700 provided with sand that primarily filters a predetermined amount through a discharge pipe to which a flowmeter is connected.

상기 모래여과조(700)를 거친 처리수는 2차적인 필터작용을 위해 활성탄이 구비된 활성탄여과조(800)에 의해 여과되어 방류관(810)을 통해 방류수가 배출되는 것을 구비되어 캐비넷형상의 하우징(900)내부에 상기 모든 구조물이 집약적으로 구비되는 집약적 폐수처리장치(100)에 관한 것이다.The treated water having passed through the sand filtration tank 700 is filtered by an activated carbon filtration tank 800 equipped with activated carbon for a secondary filter action, and discharged water is discharged through the discharge pipe 810. 900 refers to an intensive wastewater treatment apparatus 100 in which all the structures are intensively provided therein.

상기 집수조(200)에서 공급되는 폐수가 반응응집조(300)에 유입되어 동시에 정량펌프(370)에 의해 유입되는 반응제공급탱크(350)의 반응제와 응집제공급탱크(360)의 응집제를 반응응집조(300)에 교반기(310)에 의해 혼합되는 것에 있어서, 상기 반응응집조(300)내부에 하단부의 일측에 공기공급장치인 블로워(320)를 설치하여 폐수, 반응제, 응집제를 혼합시켜 폐수와 반응제와의 반응을 활성화하기 위해 산소를 공급해주며 동시에 응집제의 투입으로 폐수와의 응결 및 응집이 원활히 반응하도록 하기 위해서이며 또한, 반응응집조(300)에서 폐수가 반응제와 응집제와의 반응하는 유용한 반응시간에 있어 오랜시간동안 폐수가 체류함에 있어서 발생되는 악취를 반응응집조(300)내에 공기의 공급함에 있어 악취를 방지할 수 있는 것으로 반응응집조(300)내부에 블로워를 설치하여 산소를 공급해주는 공기공급장치로 블러워(320)를 구비하는 것을 제공하고 있다.Waste water supplied from the sump tank 200 is introduced into the reaction agglomeration tank 300 and at the same time reacts the reactant of the reactant supply tank 350 and the flocculant of the flocculant supply tank 360 which are introduced by the metering pump 370. In the mixing tank 300 is mixed by the stirrer 310, a blower 320 as an air supply device is installed on one side of the lower end in the reaction agglomeration tank 300 to mix the wastewater, the reactant, and the flocculant. In order to supply oxygen to activate the reaction between the wastewater and the reactant and at the same time, the coagulation and coagulation of the wastewater with the addition of the coagulant reacts smoothly. Blower in the reaction agglomeration tank 300 to prevent odor in supplying air into the reaction agglomeration tank 300 for the odor generated by waste water for a long time in the useful reaction time to react. It provides a blower 320 as an air supply device for supplying oxygen to install.

또한, 반응응집조(300)에 구비된 블러워(320)는 공기공급라인(340)을 통해 반응제공급탱크(350)와 응집제공급탱크(360)로 공기를 유입시켜 반응제와 응집제의 장시간 탱크내에 존재시 무기침전물이 생길 수 있어 블러워(320)를 통해 공급되는 공기발생으로 반응제와 응집제 화합물의 침전물이 발생되는 것을 억제하는 공기발생의 공기공급라인(340)을 설치하여 구비되는 것을 제공할 수 있다. 상기 반응제공급탱크(350)와 응집제공급탱크(360)에 별도의 블러워(320)를 설치하는 것이 아니라 반응응집조(300)에 설치한 블러워를 통해 공기공급라인(340)만 별도로 분리하여 각각의 반응제공급탱크(350)와 응집제공급탱크(360)로 공급하는 것을 말한다.In addition, the blower 320 provided in the reaction agglomeration tank 300 flows air into the reactant supply tank 350 and the flocculant supply tank 360 through the air supply line 340 to provide a long time of the reactant and the flocculant. Inorganic precipitates may be generated when present in the tank, and the air supply line 340 may be installed to suppress generation of precipitates of the reactant and flocculant compounds due to the generation of air supplied through the blower 320. Can provide. Instead of installing a separate blower 320 in the reactant supply tank 350 and the flocculant supply tank 360, the air supply line 340 is separately separated through the blower installed in the reaction coagulation tank 300. By means of supplying to each of the reactant supply tank 350 and the flocculant supply tank 360.

또한, 반응제공급탱크(350)와 응집제공급탱크(360)에는 반응제와 응집제의 유입되는 양을 제어하기 위해 정량펌프(370)가 설치되어 있으며, 상기 정량펌프(370)는 반응응집조(300)에 설치된 PH제어기(330)에 의해 제어되도록 되어 있으며, 이는 반응제와 응집제가 일정량을 제어하는 정량펌프(370)를 컨트롤하기 위한 것으로 반응제와 응집제가 반응응집조(300)에 투입되는 양을 결정하는 수단으로 PH제어기에 의해 그 투입양을 결정하도록 하는 것이다.In addition, the reagent supply tank 350 and the flocculant supply tank 360 is provided with a metering pump 370 to control the amount of the reactant and the flocculant inflow, the metering pump 370 is a reaction coagulation tank ( It is to be controlled by the PH controller 330 installed in 300, which is to control the metering pump 370 to control a certain amount of the reactant and flocculant is injected into the reaction coagulation tank (300) The means for determining the amount is to determine the input amount by the PH controller.

상기 반응응집조(300)에서 폐수가 처리수와 슬러지로 분리되어 있는 혼합수가 침전조(400)에 공급되고, 도 5는 본 발명에 따른 집약적 페수처리장치중에 침전 조 내부에 처리수와 슬러지가 분리되는 것을 나타낸 개념단면도에 나타낸 바와 같이 상기 침전조(400)에 공급된 혼합수는 침전조(400) 내부로 그대로 자유낙하하는 것이 아니라 혼합수의 유량에 흐름을 더욱 안정적으로 낙하를 유도하는 도 4에 나타낸 침전조의 내부단면도와 도 6에 나타낸 갈매기형 바플(baffle)의 확대사시도와 같이 수직방향으로 다수 구획하며 양측면이 침전조(400)의 내부양측면에 용접에 의해 접합되어 구비된 갈매기형상의 갈매기형 바플(baffle)(440)을 설치하고, 상기 갈매기형 바플(baffle)(440)의 형상은 상·하부에 일정길이만큼 수직면(440a)을 가지고 있으며 상·하부사이에는 일정길이의 예각면(440b)과 예각면(440b)과 같은 길이의 둔각면(440c)이 ">"형상으로 연결되어 구비되고, 전체 갈매기형 바플(baffle)(440)형상의 모양은 "

Figure 112005508331605-pat00009
" 형태이고, 상기 혼합수가 갈매기형 바플(baffle)(440)에 낙하되어 그 형상의 면적과 방향에 따라 혼합수가 안정적으로 침전조(400)의 하부로 낙하를 하게 되어 낙하된 혼합수가 서로 혼합된 형태로 존재하는 것이 아니라 처리수와 슬러지의 상분리가 형성되어 슬러지는 바닥으로 가라앉게 되며 처리수는 슬러지상부로 뜨는 원리로 작용하게 된다.In the reaction agglomeration tank 300, the mixed water in which wastewater is separated into treated water and sludge is supplied to the settling tank 400, and FIG. As shown in the conceptual sectional view showing that the mixed water supplied to the settling tank 400 is shown in Figure 4 to induce a flow more stably drop in the flow rate of the mixed water rather than freely falling into the settling tank 400 as it is The inner sectional shape of the sedimentation tank and the enlarged perspective view of the chevron baffle shown in FIG. baffle 440 is installed, and the shape of the chevron baffle 440 has a vertical surface 440a at a predetermined length in the upper and lower portions, and a constant between the upper and lower portions. Its sharp-shaped surface (440b) and the acute angle side length obtuse angle surface (440c) is ">", and having the like connected to, full chevron bapeul (baffle) (440), such as (440b) is shaped "
Figure 112005508331605-pat00009
Form, the mixed water is dropped into the chevron baffle (440) and the mixed water is stably dropped to the lower portion of the settling tank 400 according to the area and the direction of the shape is mixed with each other Rather than exist as the phase separation of the treated water and sludge is formed, the sludge sinks to the bottom and the treated water acts on the principle of floating to the top of the sludge.

상기 갈매기형은 바플(baffle)(440)은 침전조(400) 내부에 하나이상이 설치되어 있으며, 이는 혼합수에 유입되는 유량의 흐름을 더욱 안정적으로 하기 위함이다.The chevron baffle (440) is provided with one or more inside the sedimentation tank 400, which is to make the flow of the flow rate flowing into the mixed water more stable.

또한, 갈매기형 바플(baffle)(440)을 침전조(400) 내부에 설치하여 혼합수에 함유된 슬러지의 침전시간을 증가시켜 침전효과를 높이고 혼합수에 함유된 미세한 슬러지까지 침전조(400) 하부에 침전되도록 유도하는 갈매기형 바플(baffle)(440)로서 폐수처리 효율을 높이는 효과를 가져온다.In addition, by installing a gull baffle (440) inside the settling tank 400 to increase the settling time of the sludge contained in the mixed water to increase the settling effect and to the fine sludge contained in the mixed water in the bottom of the settling tank (400) As a chevron baffle 440 to induce sedimentation, the wastewater treatment efficiency is increased.

상기 침전조(400)내부 하부에 가라앉은 슬러지는 침전조(400) 하부에 구비된 제2배출관(430)을 통해 배출되며, 배출된 슬러지는 임시저장하는 슬러지저장탱크(600)에 저장되며 이는 침전조(400)에서 배출되는 슬러지의 양은 연속적으로 발생되는 것이 아니라 침전조(400) 내부의 하부에 일정량의 슬러지가 쌓이게 되며 배출하는 방식으로 상기 배출된 슬러지는 임시로 슬러지저장탱크(600)에 저장하게 된다.The sludge settled in the lower part of the settling tank 400 is discharged through the second discharge pipe 430 provided in the settling tank 400, the discharged sludge is stored in the sludge storage tank 600 for temporary storage, which is a settling tank ( The amount of sludge discharged from 400 is not generated continuously, but a predetermined amount of sludge is accumulated in the lower part of the settling tank 400, and the discharged sludge is temporarily stored in the sludge storage tank 600 by discharging.

상기 슬러지저장탱크(600)에서 저장된 슬러지를 탈수하기 위해 탈수기(650)를 거치며, 이는 슬러지에 수분이 함유되어 있어 대지중에 노출시 오염된 침출수가 다시 방출되어 토양 및 수질을 오염시킬 수 있으며 수분이 함유된 슬러지의 양을 최소화하기 위해 탈수기(650)에 의해 수분을 제거한 다음 최종슬러지를 배출하는 슬러지배출관(660)를 통해 최종슬러지저장탱크로 이송하게 된다.The dehydrator 650 is passed to dewater the sludge stored in the sludge storage tank 600. The sludge contains moisture, and when exposed to the ground, contaminated leachate may be released again to contaminate soil and water quality. In order to minimize the amount of sludge contained, water is removed by the dehydrator 650 and then transferred to the final sludge storage tank through the sludge discharge pipe 660 for discharging the final sludge.

침전조(400)에서 배출되는 처리수의 정화공정은 상기 침전조(400)에 처리수가 배출되는 제1배출관(420)이 연결되어 있는 공간주위에 "└"형태로 제1배출관(420) 연결주위에 용접처리되어 부착되며 전체적인 형상이 1-8mm의 타공(510)으로 이루어진 판상결합체며 상단부는 톱니(520)가 형성되어 있으며 처리수에 함유된 미처리된 슬러지와 부유물을 처리하기 위한 타공차단막(500)이다.Purification process of the treated water discharged from the sedimentation tank 400 is connected to the first discharge pipe 420 in the form of "└" around the space where the first discharge pipe 420 is discharged to the sedimentation tank 400 is connected Welded and attached, the overall shape is a plate-shaped assembly consisting of a hole (510) of 1-8mm and the upper end is formed with a saw tooth 520, the perforated barrier membrane 500 for treating untreated sludge and suspended solids contained in the treated water to be.

도 7은 타공차단막의 확대사시도로 상기 제1배출관(420) 주위에 구비된 타공차단막(500)을 통해 처리수가 제1배출관(420)을 통해 배출되는 처리수는 유량계가 연결된 배출라인을 통해 일정량을 1차적으로 필터작용을 하는 모래가 구비된 모래여과조(700)에 의해 여과되고, 상기 모래여과조(700)를 거친 처리수는 2차적인 필터작용을 위해 활성탄이 구비된 활성탄여과조(800)에 의해 여과되어 방류관(810)을 통해 방류수가 배출되는 것으로 처리수가 필터에 의해 정화작용으로 방류수로 배출되는 것이다.7 is an enlarged perspective view of the perforated barrier membrane, through which the treated water is discharged through the first discharge tube 420 through the perforated barrier membrane 500 provided around the first discharge tube 420, through a discharge line to which a flowmeter is connected. It is filtered by the sand filtration tank 700 is provided with sand to filter primarily, the treated water passed through the sand filtration tank 700 is activated carbon filtration tank 800 equipped with activated carbon for the secondary filter action The filtered water is discharged through the discharge pipe 810 and the treated water is discharged to the discharged water by the filter by the purification operation.

상기 반응응집조(300)에서 공급되는 혼합수가 처리수와 슬러지로 분리되어 슬러지를 침전시키고 처리수를 배출하는 구조물인 침전조(400)는 하나이상이 설치되어 집약적 폐수처리장치(100)에 구비되는 것을 제공할 수 가 있다.The sedimentation tank 400, which is a structure for separating the mixed water supplied from the reaction agglomeration tank into treated water and sludge to precipitate sludge and discharging the treated water, is installed in the intensive wastewater treatment apparatus 100. Can provide.

이는 폐수의 정화를 극대화할 수 있는 것으로 폐수처리 능력을 원활히 작용하여 폐수에 함유된 각종 슬러지와 처리수를 완벽하게 분리하기 위해 하나이상의 침전조를 구비하여 제공할 수 있다.This can maximize the purification of the waste water can be provided with one or more sedimentation tank to completely separate the various sludges and the treated water contained in the waste water by operating the waste water treatment ability smoothly.

이상에서 살펴본 바와같이 본 발명은 개별적으로 구성된 여러단계의 폐수처리장치를 하나의 폐수처리시설에 집약적으로 형성하므로서, 세차장 및 유리가공과 같이 소량의 폐수를 배출하는 업소의 설치나 소규모 기업체에 배출되는 폐수의 처리장소에 설치하고 그 설치비용이 저렴하며 좁은 공간에서도 설치가 용이한 장점이 있다.As described above, the present invention is to form the wastewater treatment apparatus of several stages configured separately in one wastewater treatment facility, so that it is discharged to the installation of small businesses such as car washes and glass processing, or to small businesses. It is installed at the wastewater treatment site, and its installation cost is low, and it is easy to install even in a narrow space.

또한, 폐수처리를 장치에서 기존의 침전조의 효능을 더욱 향상시킨 것으로 폐수에 함유된 슬러지의 침전효과를 높여 미세한 슬러지까지 침전시킬 수 있는 갈매기형 바플(baffle)을 설치함으로서 슬러지의 침전효과를 높일 수 있도록 하였다.In addition, by improving the efficacy of the existing sedimentation tank in the wastewater treatment device, the sedimentation effect of the sludge can be enhanced by installing a gull-shaped baffle that can precipitate fine sludge by increasing the sedimentation effect of the sludge contained in the wastewater. It was made.

Claims (3)

캐비넷형상을 가지고 있는 하우징(900)내부에 폐수처리시설이 집약적인 구비되는 집약적 폐수처리장치(100)에 있어서,In the intensive wastewater treatment apparatus 100 in which a wastewater treatment facility is intensively provided in a housing 900 having a cabinet shape, 폐수의 원수를 저장하는 집수조(200)와,A water collecting tank 200 for storing raw water of wastewater, 상기 집수조(200)에서 원수펌프(210)가 설치된 원수공급관(220)을 통해 폐수를 공급받는 반응응집조(300)와,A reaction agglomeration tank 300 for receiving wastewater through a raw water supply pipe 220 in which a raw water pump 210 is installed in the water collecting tank 200; 상기 반응응집조(300)에 공급된 폐수를 처리수와 슬러지의 분리 및 응집을 위해 혼합되는 반응제와 응집제는 각각 정량펌프(370)가 설치된 반응제공급탱크(350)와 응집제공급탱크(360)에 의해 반응응집조(300)에 유입되고 폐수와의 고른 혼합을 위해 반응응집조(300)에 구비된 교반기(310)에 의해 혼합되고,The reactant and flocculant mixed with the wastewater supplied to the reaction agglomeration tank 300 for the separation and flocculation of the treated water and sludge, respectively, the reactant supply tank 350 and the flocculant supply tank 360 in which the metering pump 370 is installed. Into the reaction agglomeration tank 300 by a) and mixed by the stirrer 310 provided in the reaction agglomeration tank 300 for even mixing with the waste water, 상기 반응응집조(300)에서 처리수와 슬러지로 혼합된 혼합수가 처리수와 슬러지로 분리 및 침전되기 위해 상부의 일측에 혼합수를 공급받는 혼합수공급관(410)과 상부의 다른일측에는 처리수가 배출되는 제1배출관(420)이 있으며 하부의 일측에는 슬러지를 배출하는 제2배출관(430)이 연결되어 있는 침전조(400)와,In the reaction agglomeration tank 300, the mixed water mixed with the treated water and sludge is treated water and the mixed water supply pipe 410 receiving the mixed water on one side of the upper part in order to separate and settle the treated water and sludge. There is a first discharge pipe 420 is discharged and the settling tank 400 is connected to the second discharge pipe 430 for discharging the sludge on one side of the lower, 상기 침전조(400)의 내부 공간에는 혼합수가 혼합수공급관(410)을 통해 유입되는 유량의 흐름을 조절하여 더욱 안정적으로 혼합수가 낙하하도록 하는 수직방향으로 다수 구획하며 양측면이 침전조(400)의 내부양측면에 용접에 의해 접합되어 구비된 갈매기형상의 갈매기형 바플(baffle)(440)과,The inner space of the settling tank 400 is divided into a plurality of vertical direction to allow the mixed water to fall more stably by controlling the flow of the flow rate of the mixed water flowing through the mixed water supply pipe 410, both sides of the inner both sides of the settling tank 400 Chevron-shaped chevron baffles 440 which are joined to each other by welding, 상기 갈매기형 바플(baffle)(440)의 상·하부에 일정길이만큼 수직면(440a) 을 가지고 있으며 상·하부사이에는 일정길이의 예각면(440b)과 예각면(440b)과 같은 길이의 둔각면(440c)이 ">"형상으로 연결되어 구비되고,The upper and lower portions of the chevron baffle 440 has a vertical surface 440a by a predetermined length, and the upper and lower obtuse surfaces having the same length as the acute angle 440b and the acute angle 440b. 440c is provided connected in a ">" shape, 상기 침전조(400)에 처리수가 배출되는 제1배출관(420)이 연결되어 있는 공간주위에 "└"형태로 제1배출관(420) 연결주위에 용접처리되어 부착되며 전체적인 형상이 1-8㎜의 타공(510)으로 이루어진 판상결합체며 상단부는 톱니(520)가 형성되어 있으며 처리수에 함유된 미처리된 슬러지와 부유물을 처리하기 위한 타공차단막(500)과,Welded around the first discharge pipe 420 in the form of "└" attached to the space around the first discharge pipe 420 is discharged treatment water discharged to the sedimentation tank 400, the overall shape of 1-8mm Plate-shaped assembly consisting of the perforations 510 and the upper end has a tooth 520 is formed and the perforated barrier membrane 500 for treating untreated sludge and suspended matter contained in the treated water, 상기 침전조(400)에서 제2배출관(430)을 통해 흘러나온 슬러지를 저장하는 슬러지저장탱크(600)와,Sludge storage tank 600 for storing the sludge flowed out through the second discharge pipe 430 in the settling tank 400, 상기 슬러지저장탱크(600)에서 저장된 슬러지를 탈수하기 위해 탈수기(650)를 거쳐 최종슬러지를 배출하는 슬러지배출관(660)가 구비되고,Sludge discharge pipe 660 is provided to discharge the final sludge through the dehydrator 650 to dewater the sludge stored in the sludge storage tank 600, 상기 침전조(400)에서 배출되는 처리수는 유량계가 연결된 배출관을 통해 일정량을 1차적으로 필터작용을 하는 모래가 구비된 모래여과조(700)에 의해 여과되고,The treated water discharged from the settling tank 400 is filtered by a sand filtration tank 700 provided with sand that primarily filters a predetermined amount through a discharge pipe to which a flowmeter is connected. 상기 모래여과조(700)를 거친 처리수는 2차적인 필터작용을 위해 활성탄이 구비된 활성탄여과조(800)에 의해 여과되어 방류관(810)을 통해 방류수가 배출되는 것을 구비되어 캐비넷형상의 하우징(900)내부에 상기 모든 구조물이 집약적으로 구비되는 것을 특징으로 하는 집약적 폐수처리장치The treated water having passed through the sand filtration tank 700 is filtered by an activated carbon filtration tank 800 equipped with activated carbon for a secondary filter action, and discharged water is discharged through the discharge pipe 810. Intensive wastewater treatment apparatus, characterized in that all the above structure is provided intensively 제1항에 있어서, 침전조(400)내부에 설치된 갈매기형은 바플(baffle)(440)은 침전조(400) 내부에 하나이상이 설치되어 있어 혼합수내의 미세한 슬러지까지 침전시키고 혼합수에 유입되는 유량의 흐름을 더욱 안정적으로 하기 위해 설치되는 것을 특징으로 하는 집약적 폐수처리장치According to claim 1, wherein the gull-shaped baffle (440) installed in the sedimentation tank 400 is one or more installed in the sedimentation tank 400 is settled to fine sludge in the mixed water and flow rate flowing into the mixed water Intensive wastewater treatment device, characterized in that installed to make the flow more stable 제1항에 있어서, 반응응집조(300)에서 공급되는 혼합수가 처리수와 슬러지로 분리되어 슬러지를 침전시키고 처리수를 배출하는 구조물인 침전조(400)가 하나이상이 설치되는 것을 특징으로 하는 집약적 폐수처리장치The method of claim 1, wherein the mixed water supplied from the reaction agglomeration tank 300 is separated into treated water and sludge to settle the sludge and discharge the treated water is intensive, characterized in that one or more sedimentation tank 400 is installed Wastewater Treatment System
KR1020050059998A 2005-07-01 2005-07-01 Intensive Wastewater Treatment System Expired - Lifetime KR100628881B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020050059998A KR100628881B1 (en) 2005-07-01 2005-07-01 Intensive Wastewater Treatment System

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020050059998A KR100628881B1 (en) 2005-07-01 2005-07-01 Intensive Wastewater Treatment System

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
KR20-2004-0036800U Division KR200377629Y1 (en) 2004-12-22 2004-12-22 Compact waste water treatment apparatus

Publications (2)

Publication Number Publication Date
KR20060071838A KR20060071838A (en) 2006-06-27
KR100628881B1 true KR100628881B1 (en) 2006-10-02

Family

ID=37165208

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020050059998A Expired - Lifetime KR100628881B1 (en) 2005-07-01 2005-07-01 Intensive Wastewater Treatment System

Country Status (1)

Country Link
KR (1) KR100628881B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101431325B1 (en) 2012-08-29 2014-08-20 김영상 Waste water purification apparatus

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101157578B1 (en) * 2009-07-07 2012-06-18 고려종합건설 주식회사 Pressure and vacuum dividing waste water disposal system
CN110563107B (en) * 2019-09-23 2022-08-19 彭素荣 Sewage treatment sedimentation tank structure
KR102766888B1 (en) * 2024-07-08 2025-02-13 주식회사 디엠 System for reusing wastewater sludge generated when cutting underwater structures

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002102662A (en) 2001-08-21 2002-04-09 Togami Electric Mfg Co Ltd Livestock wastewater treatment system and solid-liquid separation method in primary settling basin, aeration tank and anaerobic tank to be used for the same
JP2002143875A (en) 2000-08-23 2002-05-21 Togami Electric Mfg Co Ltd Water or waste water or sewage treatment equipment and method of manufacturing for the same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002143875A (en) 2000-08-23 2002-05-21 Togami Electric Mfg Co Ltd Water or waste water or sewage treatment equipment and method of manufacturing for the same
JP2002102662A (en) 2001-08-21 2002-04-09 Togami Electric Mfg Co Ltd Livestock wastewater treatment system and solid-liquid separation method in primary settling basin, aeration tank and anaerobic tank to be used for the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101431325B1 (en) 2012-08-29 2014-08-20 김영상 Waste water purification apparatus

Also Published As

Publication number Publication date
KR20060071838A (en) 2006-06-27

Similar Documents

Publication Publication Date Title
KR100978939B1 (en) Remote monitoring and automatic control device for complex pollution groundwater purification
KR100905693B1 (en) Early Rainwater Treatment Unit
KR100948553B1 (en) Groundwater purifying system
KR20120022028A (en) Apparatus for treatment of first flush rainfall
KR100621193B1 (en) Pollution Purification Method of Pollution Purification System and Pollution Purification System
KR101189912B1 (en) Apparatus for Treating Waste Water
KR200377629Y1 (en) Compact waste water treatment apparatus
KR100628881B1 (en) Intensive Wastewater Treatment System
KR100984167B1 (en) Complex pollution groundwater purification treatment method and device
KR200336701Y1 (en) Polluted river-water purification system using direct aeration
KR100724778B1 (en) Wastewater Treatment System
KR100427774B1 (en) Purification method and that equipment of abandoned mine drainage
KR100960643B1 (en) Polluted water treatment device
KR101103411B1 (en) Heavy Metal Removal Device in Soil
CN212222719U (en) A kind of cleaning liquid automatic filtering processing equipment
CN108101274A (en) A kind of oils high-COD waste water pretreating process and equipment
JPH09276606A (en) Method of settling and filtering foul water and tank for settling and filtering sewage
KR20010016337A (en) Wastewater purification treatment system
KR101403882B1 (en) Water processing plant and water drainage system
KR101913415B1 (en) Multiple stage purifier of water
JP4382397B2 (en) Earth and sand cleaning device and earth and sand cleaning method
JP4396981B2 (en) Sewage treatment equipment
KR20220014631A (en) Water Purification System for water channel using Storage space
JP5080734B2 (en) Muddy water treatment method, muddy water treatment device, and seaweed paste for muddy water treatment
CN105254112A (en) Deep wastewater treatment apparatus

Legal Events

Date Code Title Description
A108 Dual application of patent
A201 Request for examination
PA0108 Dual application

Patent event code: PA01081R01D

Patent event date: 20050701

Comment text: Dual Application of Patent

PA0201 Request for examination
PG1501 Laying open of application
E701 Decision to grant or registration of patent right
PE0701 Decision of registration

Patent event code: PE07011S01D

Comment text: Decision to Grant Registration

Patent event date: 20060828

GRNT Written decision to grant
PR0701 Registration of establishment

Comment text: Registration of Establishment

Patent event date: 20060920

Patent event code: PR07011E01D

PR1002 Payment of registration fee

Payment date: 20060920

End annual number: 3

Start annual number: 1

PG1601 Publication of registration
PR1001 Payment of annual fee

Payment date: 20090721

Start annual number: 4

End annual number: 4

PR1001 Payment of annual fee

Payment date: 20100629

Start annual number: 5

End annual number: 5

PR1001 Payment of annual fee

Payment date: 20110920

Start annual number: 6

End annual number: 6

FPAY Annual fee payment

Payment date: 20120919

Year of fee payment: 7

PR1001 Payment of annual fee

Payment date: 20120919

Start annual number: 7

End annual number: 7

FPAY Annual fee payment

Payment date: 20130731

Year of fee payment: 8

PR1001 Payment of annual fee

Payment date: 20130731

Start annual number: 8

End annual number: 8

FPAY Annual fee payment

Payment date: 20160729

Year of fee payment: 11

PR1001 Payment of annual fee

Payment date: 20160729

Start annual number: 11

End annual number: 11

FPAY Annual fee payment

Payment date: 20170810

Year of fee payment: 12

PR1001 Payment of annual fee

Payment date: 20170810

Start annual number: 12

End annual number: 12

FPAY Annual fee payment

Payment date: 20190731

Year of fee payment: 14

PR1001 Payment of annual fee

Payment date: 20190731

Start annual number: 14

End annual number: 14

PR1001 Payment of annual fee

Payment date: 20240910

Start annual number: 19

End annual number: 19