KR100307260B1 - System of processing sewage - Google Patents

System of processing sewage Download PDF

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Publication number
KR100307260B1
KR100307260B1 KR1019990007702A KR19990007702A KR100307260B1 KR 100307260 B1 KR100307260 B1 KR 100307260B1 KR 1019990007702 A KR1019990007702 A KR 1019990007702A KR 19990007702 A KR19990007702 A KR 19990007702A KR 100307260 B1 KR100307260 B1 KR 100307260B1
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South Korea
Prior art keywords
valve
wastewater
blower
compartment
tank
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KR1019990007702A
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Korean (ko)
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KR19990046000A (en
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유지순
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양영희
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • 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
    • C02F7/00Aeration of stretches of water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/005Valves
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/42Liquid level

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE: A treatment system of sewage and wastewater is provided, which can treat sewage and wastewater using a single reaction tank by only actuating pump and blower through control part. Plural reaction tanks set in parallel can be operated alternately, thus eliminating any downtime of the facilities and reducing malfunction. CONSTITUTION: The system comprises a screen tank(200), a reaction tank(210) and a control part(270). The reaction tank(210) is composed of No.1 compartment(214) and No.2 compartment(218). Water screened at the screen tank(200) enter the No.1 compartment(214), in which water level is sensed by a level sensor(226), through a motorized valve(222) controlled by the control part(270), flow to No.2 compartment through the under passage, and discharged through the discharge hole(216) set at the top. To the No.1 and No.2 compartment, compressed air is fed through air spargers(240).

Description

하/폐수 처리 시스템{SYSTEM OF PROCESSING SEWAGE}Sewage / Wastewater Treatment System {SYSTEM OF PROCESSING SEWAGE}

본 발명은 하/폐수처리 시스템에 관한 것으로, 특히 일측 상부에 처리수유출구가 고정 설치된 반응조를 이분하여 복수개 격실을 형성하여 블로워의 동작에 따라 상기 단일 반응조에서 폭기와 침전이 동시에 이루어지도록 한 뒤 처리수유출구 반대측 격실의 공기압에 의하여 처리수가 처리수유출구로 배출되도록 함과 아울러 상기 반응조를 병렬로 복수개 설치하여 각각 교번동작시킴으로써, 설치비용과 공간이 감소되도록 하고 처리효율이 향상되도록 하는 하/폐수처리 시스템에 관한 것이다.The present invention relates to a sewage / wastewater treatment system, and in particular, a plurality of compartments are formed by dividing a reaction tank in which a treatment water outlet is fixed at an upper portion thereof so that aeration and precipitation are simultaneously performed in the single reactor according to the operation of a blower. The sewage / wastewater treatment system allows the treated water to be discharged to the treated water outlet by the air pressure of the compartment opposite to the water outlet, and installs a plurality of reaction tanks in parallel so that the installation cost and space are reduced and the treatment efficiency is improved. It's about the system.

종래의 하/폐수 처리시스템은 소정의 하수 및 폐수처리장치를 통하여 하수 및 폐수를 정화하여 방류하고, 이때 발생되는 슬러지를 소정의 탈수 공법을 통하여 탈수시킨 후, 매립하거나 소각하여 처리하였는데, 그 실시 예를 하기에서 도 1 과 도 2 및 도 3을 참조하여 간략적으로 살펴본다.The conventional sewage / wastewater treatment system purifies and discharges sewage and wastewater through predetermined sewage and wastewater treatment devices, and dewatered sludge generated through a predetermined dehydration method, and then landfilled or incinerated and treated. An example will be briefly described with reference to FIGS. 1, 2, and 3.

우선, 도 1은 종래의 폐수처리 장치 및 과정을 나타내는 블록도로써, 폐수유입구(12)를 통하여 스크린조(10)로 유입된 폐수는 스크린(14)에 의하여 비교적 부피가 큰 협잡물 및 부유성 물질이 제거된 후, 유량 조절조(20)에 의하여 최초 침전지(30)로 적정량이 유입되어 일정시간동안 체류되는데, 이와 같은 체류과정에 의하여 최초 침전지(3)의 저부에는 폐수에 포함된 현탁고형물들이 중력에 의하여 침전되고 상부에는 액상층이 형성되어 저부에 침전된 슬러지는 농축조(60)로 공급되고 상층의 액상층은 폭기조(40)로 유입되어 폭기되는데, 이때 상기 폭기조(40)에서는 최종 침전지(30)로부터 반송된 슬러지와 액상층의 혼합이 폭기와 동시에 이루어진다. 그리고, 상기한 바와 같이 폭기 및 혼합을 거친 폭기조(40)내의 폐수는 최종 침전지(50)로 유입되며, 최종 침전지(50)에서는 유입된 폐수의 농도에 따른 슬러지가 저부에 침전되고 상부에는 액상 부분이 형성되는데, 저부의 슬러지중 일부는 폭기조(40)로 반송되고, 나머지 슬러지는 농축조(60)로 유입되어 최초 침전지(30)로부터 발생된 슬러지와 함께 농축조(60)에서 농축된 후, 탈수기(70)에 의하여 탈수되어 슬러지 케익으로 배출되며, 상기 최종 침전지(50)의 상부 액상층은 외부로 배출된다.First, Figure 1 is a block diagram showing a conventional wastewater treatment apparatus and process, wastewater introduced into the screen tank 10 through the wastewater inlet 12 is a relatively bulky contaminants and suspended solids by the screen (14) After this is removed, an appropriate amount flows into the initial settling basin 30 by the flow control tank 20 and stays for a predetermined time. At the bottom of the initial settling basin 3, the suspended solids contained in the wastewater are retained. Sludge precipitated by gravity and the liquid layer is formed at the top to precipitate the bottom is supplied to the concentration tank 60 and the liquid layer of the upper layer is introduced into the aeration tank 40, the aeration tank 40, the final sedimentation basin ( The sludge conveyed from 30) and the liquid layer are mixed at the same time as the aeration. Then, the wastewater in the aeration tank 40 subjected to the aeration and mixing as described above is introduced into the final sedimentation basin 50, in the final sedimentation basin 50, sludge according to the concentration of the wastewater introduced into the bottom and the liquid portion at the top This is formed, some of the bottom sludge is returned to the aeration tank 40, the remaining sludge flows into the concentration tank 60 and concentrated in the concentration tank 60 together with the sludge generated from the initial settling basin 30, and then dehydrator ( 70) is dewatered and discharged to the sludge cake, the upper liquid layer of the final sedimentation basin 50 is discharged to the outside.

그리고, 종래의 하수처리장치는 상기 도 1에 나타내는 폐수처리 장치의 농축조(60)의 후단에 도 2에 나타내는 바와 같이 소화조(80)와 소화조(80)로부터 발생되는 소화가스를 처리하는 소화가스저장조(90)를 더 추가한 것으로, 상기 소화조(80)로부터 발생되는 슬러지는 탈수기(70)를 거쳐서 케익으로 배출되고, 소화가스저장조(90)의 소화가스는 보일러(95)에서 연소되어 소화조(80)를 가온(加溫)시켜주게 된다.In the conventional sewage treatment apparatus, a digestion gas storage tank for treating the digestion gas generated from the digestion tank 80 and the digestion tank 80 as shown in FIG. 2 at the rear end of the concentration tank 60 of the wastewater treatment apparatus shown in FIG. In addition to the 90, the sludge generated from the digester 80 is discharged to the cake through the dehydrator 70, the digestion gas of the digestion gas storage tank 90 is burned in the boiler (95) digestion tank (80) ) Will warm (加溫).

그러나, 상기한 바와 같은 종래의 하/폐수 처리장치 및 방법에 의하면 다수의 각각 다른 처리공정이 필요하여 고도의 유지관리기술이 필요한 문제점이 있고, 최총 침전지로부터 폭기조로 적정량의 슬러지를 반송하여야 하는 불편이 있으며, 만약 공정중 어느 부분에 이상이 발생될 경우 완벽하게 정화되지 않은 처리수가 유출되게 되는 문제점이 발생되었다. 또한, 별도의 탈질, 탈인 공정이 필요하였다.However, according to the conventional sewage / wastewater treatment apparatus and method as described above, a number of different treatment processes are required, and thus a high level of maintenance technology is required. There is a problem that if the abnormality occurs in any part of the process, the treated water that is not completely purified flows out. In addition, a separate denitrification and dephosphorization process was required.

한편, 도 3은 종래의 다른 하수 처리 시스템을 나타내는 도면으로서, 일측에 하수 유입구(112)가 형성되고 타측에 처리수를 배출하기 위한 데칸트(dacant; 114)가 설치된 하나의 반응조(110)로 구성되며, 상기 반응조(110)의 운전을 살펴보면 하수는 지속적으로 반응조(110)내로 유입되며 반응조(110)내부가 기 설정된 소정수위가 될 때까지 폭기가 진행되고, 상기한 기 설정된 소정 수위가 되면 기 설정된 소정 기간동안 산소 공급이 중단되는데 이때 반응조(110)내의 현탁고형물들은 중력에 의하여 반응조(110)의 저부에 침전되고 상부에는 액상층이 형성된다. 상기한 바와 같이 고형물의 침전이 종료되면 데칸트(114)가 동작되어 반응조(110)내의 상부 액상층의 처리수를 외부로 유출시키며, 상기한 폭기과정과 침전과정 및 처리수 배출과정은 순차적으로 계속 반복된다.On the other hand, Figure 3 is a view showing another conventional sewage treatment system, a sewage inlet 112 is formed on one side and a reactor (110) provided with a decant (114) for discharging the treated water on the other side When the operation of the reaction tank 110 is configured, the sewage is continuously introduced into the reaction tank 110 and the aeration proceeds until the inside of the reaction tank 110 reaches a predetermined predetermined level. The supply of oxygen is stopped for a predetermined period of time. At this time, suspended solids in the reactor 110 are precipitated at the bottom of the reactor 110 by gravity and a liquid layer is formed at the top. As described above, when the precipitation of the solid is finished, the decant 114 is operated to discharge the treated water of the upper liquid layer in the reaction tank 110 to the outside, and the aeration process, the precipitation process, and the discharged water process are sequentially performed. Repeatedly.

그러나, 상기한 바와 같은 하수처리에 의하면, 단일 반응조를 사용하므로 반응조(110)에 이상이 발생될 경우 하수를 처리할 수 없게 되는 문제점이 있으며, 처리수를 외부로 유출하기 위하여 데칸트(114)를 설치하여야 하므로, 설치비용이 증가하게 되고 상기 데칸트(114)를 운용하기 위한 별도의 시스템이 필요한 문제점이 있었다.However, according to the sewage treatment as described above, since a single reaction tank is used, when an abnormality occurs in the reaction tank 110, there is a problem in that the sewage cannot be treated, and the decant 114 to flow out the treated water to the outside. Since it must be installed, the installation cost is increased and there was a problem that a separate system for operating the Decant 114 is required.

상술한 바와 같은 종래의 문제점을 해결하기 위한 본 발명의 목적은 일측상부에 처리수유출구가 형성된 반응조를 폐수유입구와 연결된 밀폐 격실과 이에 연결된 처리수 유출구측 격실로 이분하고 각 격실에는 중간에 밸브가 설치되어 블로워와 연결된 배관을 소정형상으로 설치하여 블로워 및 밸브의 개/폐상태에 따라 단일 반응조에서 폭기와 침전이 이루어지도록 함과 아울러 침전 후 밀폐 격실의 압력에 의하여 처리수가 처리수유출구를 통하여 외부로 유출되도록 하며, 상기 반응조를 병렬로 복수개 설치하여 각각 교번동작시킴으로써, 처리효율이 향상되도록 함과 아울러 설치비용과 장소가 감소되도록 하는 하/폐수처리 시스템을 제공하는 데 있다.An object of the present invention for solving the conventional problems as described above is to divide the reaction tank in which the treatment water outlet is formed on one side into a sealed compartment connected to the wastewater inlet and the treatment water outlet side compartment connected thereto, and each valve has a valve in the middle. The pipe connected to the blower is installed in a predetermined shape to allow aeration and precipitation in a single reactor according to the open / closed state of the blower and valve, and the treated water is discharged through the treated water outlet through the pressure of the sealed compartment after settling. It is to provide a sewage / wastewater treatment system to be discharged to, and by installing a plurality of the reaction vessel in parallel to each alternate operation, to improve the treatment efficiency and to reduce the installation cost and location.

도 1은 종래의 하수처리 시스템을 나타내는 도면1 is a view showing a conventional sewage treatment system

도 2는 종래의 폐수처리 시스템을 나타내는 도면2 is a view showing a conventional wastewater treatment system

도 3은 종래의 다른 하수처리 시스템을 나타내는 도면3 is a view showing another conventional sewage treatment system

도 4는 본 발명에 따른 하/폐수 처리시스템을 나타내는 도면4 shows a sewage / wastewater treatment system according to the present invention.

도 5는 본 발명에 따른 반응조를 병렬로 복수개 설치한 예를 나타내는 평면도5 is a plan view showing an example in which a plurality of reaction tanks in parallel are installed according to the present invention.

도 6은 본 발명에 따른 하/폐수 처리시스템의 동작을 나타내는 순서도6 is a flow chart showing the operation of the sewage / wastewater treatment system according to the present invention

* 도면의 주요부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings

200 : 스크린조 210 : 반응조200: screen tank 210: reactor

214, 218 : 격실 226 : 수위검출센서214, 218: compartment 226: water level sensor

222, 242, 252, 262 : 밸브 230 : 블로워222, 242, 252, 262: valve 230: blower

224, 240, 250, 260 : 관 270 : 제어부224, 240, 250, 260: tube 270: control unit

상기한 목적을 달성하기 위한 본 발명의 실시 예를 도면을 참조하여 하기에서 상세히 설명한다.Embodiments of the present invention for achieving the above object will be described in detail below with reference to the drawings.

도 4는 본 발명에 따른 하/폐수 처리 시스템을 나타내는 도면이고, 도 5는 본 발명에 따른 반응조의 병렬설치예를 나타내는 평면도이고, 도 6은 본 발명에 따른 하/폐수 처리 시스템의 동작을 나타내는 순서도이다.4 is a view showing the sewage / wastewater treatment system according to the present invention, Figure 5 is a plan view showing an example of parallel installation of the reaction vessel according to the present invention, Figure 6 shows the operation of the sewage / wastewater treatment system according to the present invention Flowchart.

우선, 본 발명에 따른 복수개의 반응장치는 구성이 동일하므로 도 4에는 하나의 반응장치를 도시하였으며 이에 따른 본 발명에 따른 하/폐수 처리시스템의 구조를 살펴보면, 유입되는 하/폐수(이하 폐수)에서 큰 부유물을 제거하는 스크린조(200)를 포함하는 하/폐수 처리 시스템에 있어서, 폐수 유입구(212)가 상부 종단 인접부에 형성되어 일측 하단부만 개방형성된 제 1 격실(214)과 상기 제 1 격실(214)과 연통되어 상부에 처리수 유출구(216)가 형성된 제 2 격실(218)로 구성되는 반응조(210)와, 상기 스크린조(200)와 폐수유입구(212)사이를 연결하며 중간에 전동밸브(222 ; 이하 폐수유입관밸브)가 설치된 폐수유입관(224)과, 상기 반응조(210)내에 설치되어 폐수의 수위를 검출하는 수위검출센서(226)와, 반응조(210)의 외부에 설치된 블로워(230)와, 중간에 유로의 개폐를 제어하는 전동밸브(242 ; 이하 산기관밸브)가 설치되어 상기 제 1, 2격실(214)(218)의 하부와 블로워(230)를 연결하는 산기관(240)과, 중간에 유로의 개폐를 제어하는 전동밸브(252 ; 이하 공기배출관밸브)가 설치되어 상기 제 1 격실(214)에 연통되도록 설치되는 공기배출관(250)과, 중간에 유로의 개폐를 제어하는 전동밸브(262 ; 이하 가압공기관밸브)가 설치되어 블로워(230)와 상기 공기배출관(250)의 공기배출관밸브(252)와 제 1격실(214) 사이를 연결하는 가압공기관(260)으로 구성되는 복수개의 반응장치(265)(265a)를 도 5에 나타내는 바와 같이 병렬로 설치하고, 상기 수위검출센서(226)로부터 출력되는 신호를 기준으로 하여 다수개의 밸브(222)(242)(252)(262)와 블로워(230)(230a)의 동작을 제어하는 제어부(270)로 구성되는 것으로, 상기 제어부(270)는 일측 반응장치(265)가 폐수유입과정을 수행하는 동안 다른 반응장치(265a)는 폭기와 침전 및 배출과정을 수행하도록 하여 휴지기간없이 폐수가 처리되도록 하는데, 상기에서 폐수유입과정은 폐수유입관밸브(222)와 산기관밸브(242)와 공기배출관밸브(252)를 오픈시키고 가압공기관밸브(262)를 클로즈시켜 블로워(230)를 동작시켜 폐수가 반응조(210)로 유입됨과 동시에 폭기가 이루어지도록 하는 과정이고, 폭기과정은 폐수유입관밸브(222)를 클로즈한 후 블로워(230)를 일정시간 더 동작시키는 과정이고, 침전과정은 블로워(230)를 중지시켜 폭기된 폐수가 일정시간동안 침전되도록 하는 과정이고, 배출과정은 산기관밸브(242)와 공기배출관밸브(252)를 클로즈시키고 공기가압관밸브(262)를 오픈시킨 후 블로워(230)를 구동시켜 처리수를 배출하는 과정이다.First, since a plurality of reactors according to the present invention have the same configuration, one reactor is shown in FIG. In the sewage / wastewater treatment system including a screen tank 200 for removing a large float from the wastewater, the wastewater inlet 212 is formed in the upper end adjacent to the first compartment 214 and the first opening is formed only one side lower end A reaction tank 210 composed of a second compartment 218 communicating with the compartment 214 and having a treatment water outlet 216 formed thereon, and connecting the screen tank 200 and the waste water inlet 212 therebetween. A wastewater inlet pipe 224 provided with an electric valve 222 (hereinafter referred to as a wastewater inlet pipe valve), a water level detection sensor 226 installed in the reactor 210 to detect the level of wastewater, and an outside of the reactor 210. Blower 230 provided and opening and closing of flow path in the middle An electric valve 242 (hereinafter, referred to as an diffuser valve) is installed to connect the lower part of the first and second compartments 214 and 218 and the blower 230 to open and close the flow path. A control valve (252; air discharge pipe valve) is provided to control the air discharge pipe 250 is installed so as to communicate with the first compartment 214, and an electric valve (262; A plurality of reactors (265) is provided is composed of a pressurized air pipe 260 is installed between the blower 230 and the air discharge pipe valve 252 and the first compartment 214 of the air discharge pipe 250 ( 265a are installed in parallel as shown in Fig. 5, and a plurality of valves 222, 242, 252, 262 and blowers 230 (based on the signal output from the water level detection sensor 226) are used. It consists of a control unit 270 for controlling the operation of 230a, the control unit 270 is one side reaction apparatus 265 wastewater During the inflow process, another reactor 265a performs aeration, sedimentation, and discharge processes so that the wastewater is treated without a rest period. The wastewater inflow process includes a wastewater inlet pipe valve 222 and an diffuser valve ( 242) and the air discharge pipe valve 252 is opened and the pressurized air valve 262 is closed to operate the blower 230 so that the waste water is introduced into the reaction tank 210 and the aeration is made at the same time, the aeration process waste water After closing the inlet valve 222, the blower 230 is further operated for a predetermined time, and the precipitation process stops the blower 230 to allow the aerated waste water to settle for a predetermined time, and the discharge process is acid. After the engine valve 242 and the air discharge pipe valve 252 are closed and the air pressure pipe valve 262 is opened, the blower 230 is driven to discharge the treated water.

한편, 상기한 구성에서 반응조(210)의 하부는 도시하지는 않았지만 농축조 및 탈수기와 연결된다.On the other hand, the lower portion of the reaction tank 210 in the above configuration is connected to the concentration tank and dehydrator although not shown.

그리고, 도면중 미설명부호 219는 제 1 격실(214)의 상부에 형성된 뚜껑이고, 228은 반응조(210)의 폐수가 스크린조(200)로 역류되는 것을 방지하기 위한 체크밸브이다.In addition, reference numeral 219 in the figure is a lid formed on the upper portion of the first compartment 214, 228 is a check valve for preventing the waste water of the reaction tank 210 flows back to the screen tank 200.

상기한 바와 같이 구성된 하/폐수 처리 시스템의 일측 반응장치(265)(265)의 동작을 도 6의 순서도를 참조하여 하기에서 보다 상세하게 살펴보는데, 다른 반응장치(265a)의 동작은 상기 일측 반응장치(265)가 폐수유입과정을 수행할 경우 폭기와 침전 및 배출과정을 실행하고, 상기 일측 반응장치(265)가 폭기와 침전 및 배출과정을 수행하는 동안 폐수유입과정을 수행하는 것으로 자세한 설명은 생략한다.The operation of one side reaction apparatus 265 and 265 of the sewage / wastewater treatment system configured as described above will be described in more detail below with reference to the flowchart of FIG. 6, and the operation of the other reaction apparatus 265a is the one side reaction. When the apparatus 265 performs the wastewater inflow process, aeration and precipitation and discharge processes are executed, and the one side reaction apparatus 265 performs the wastewater inflow process while performing the aeration and precipitation and discharge processes. Omit.

우선, 제어부(270)는 폐수유입관밸브(222)와 산기관밸브(242)와 공기배출관밸브(252)를 오픈(OPEN)시키고 가압공기관밸브(262)는 클로즈(CLOSE)시킴과 아울러 블로워(230)를 동작시켜서 반응조(210)내부로 폐수를 유입시킴과 동시에 폭기과정을 수행한다(S101). 이때, 상기 블로워(230)에 의하여 밸브(242)가 오픈된 산기관(240)를 통하여 제 1격실(214)로 유입되어 폭기된 공기는 공기배출관밸브(252)가 오픈되어 있기 때문에 공기배출관(250)을 통하여 외부로 배출되고, 이에 따라 제 1 격실(214)내부의 압력이 상승되는 일이 발생하지 않게 되는 것이다.First, the control unit 270 opens the wastewater inlet pipe valve 222, the diffuser valve 242, and the air discharge pipe valve 252, and closes the pressurized air valve 262. By operating 230, the wastewater is introduced into the reactor 210 and the aeration process is performed at the same time (S101). At this time, the air introduced into the first compartment 214 through the diffuser 240 in which the valve 242 is opened by the blower 230 and aerated is air discharge pipe valve 252 because the air discharge pipe ( It is discharged to the outside through the 250, so that the pressure inside the first compartment 214 does not occur.

그리고, 제어부(270)는 상기 스텝 S101을 수행하면서 수위검출센서(226)로부터 출력되는 신호를 기준으로 하여 반응조(210)내부의 수위가 기 설정된 소정치(X1) 이상인가를 판단(S102)하여, 반응조(210)내부의 수위가 기 설정된 소정치(X1) 이하라고 판단되면 상기 스텝 S101을 반복실행하고, 반응조(210)내부의 수위가 폭기과정을 진행하기 위하여 설정된 수위(X1)이상이라고 판단되면 폐수유입관밸브(222)를 클로즈시키고 블로워(230)를 기설정된 소정시간(폭기를 위하여 설정된 시간)동안 더 동작시킨 후 블로워(230)의 동작을 정지시켜 소정시간(슬러지가 완벽하게 침전되도록 하는 시간)을 경과시킴으로써, 폐수 중에서 중량을 가지는 슬러지는 반응조(210)의 저부로 침전되도록 하고 반응조(210)상부에는 액상층이 형성되도록 한다.(S103)Then, the controller 270 determines whether the water level inside the reaction tank 210 is equal to or greater than the predetermined value X1 based on the signal output from the water level detection sensor 226 while performing the step S101 (S102). If the water level in the reactor 210 is determined to be equal to or less than the predetermined value X1, the step S101 is repeated, and the water level in the reactor 210 is determined to be equal to or higher than the water level X1 set to proceed with the aeration process. When the waste water inlet pipe valve 222 is closed and the blower 230 is further operated for a predetermined time (set time for aeration), the operation of the blower 230 is stopped so that the sludge is completely settled. Time), the sludge having a weight in the waste water is allowed to settle to the bottom of the reactor 210 and a liquid layer is formed on the reactor 210. (S103)

상기한 스텝 S103을 수행한 후 제어부(270)는 산기관밸브(242)와 공기배출관밸브(252)를 클로즈시키고 가압공기관밸브(262)를 오픈시킨 후 블로워(230)를 동작시켜서 제 1 격실(214)내부의 공기압이 상승되도록 함으로써, 제 1 격실(214)내의 처리수가 공기압에 의하여 제 2격실(218)로 배출되어 처리수유출구(216)를 통하여 외부로 배출되도록 하고(S104), 이때 수위검출센서(226)로부터 출력되는 신호를 기준으로 하여 반응조(210)내의 수위가 기 설정된 다른 소정치(상층부의 처리수만 배출되고 슬러지는 배출되지 않도록 하는 수위 ; X2)이하인지를 판단(S105)하여 반응조(210)내부의 수위가 기 설정된 소정치(X2)이상이면 상기 스텝 S104를 반복실행하고 수위가 기 설정된 소정치(X2)이하라고 판단되면 스텝 S101로 과정을 귀환한다.After performing step S103, the control unit 270 closes the diffuser valve 242 and the air discharge pipe valve 252, opens the pressurized air valve 262, and operates the blower 230 to operate the first compartment ( By increasing the internal air pressure, the treated water in the first compartment 214 is discharged to the second compartment 218 by the air pressure to be discharged to the outside through the treated water outlet 216 (S104). On the basis of the signal output from the detection sensor 226, it is determined whether or not the water level in the reaction tank 210 is lower than another predetermined value (water level so that only the treated water in the upper part is discharged and sludge is not discharged; X2) (S105). If the water level in the reactor 210 is greater than or equal to the predetermined value X2, step S104 is repeatedly executed. If the level is determined to be less than or equal to the predetermined value X2, the process returns to step S101.

한편, 다른 반응장치(265a)가 상기한 일측반응장치(265)와 교번동작되므로 휴지기간없이 유입되는 폐수를 지속적으로 처리할 수 있게 되는 것이다.On the other hand, since the other reaction device 265a is alternately operated with the one-side reaction device 265, it is possible to continuously treat the wastewater introduced without a rest period.

따라서, 본 발명에 의하면 단일 반응조로 하/폐수의 처리가 가능하게 되고 제어부가 블로워 및 밸브의 동작만 제어하면 되는 것이므로 설치비용 및 소요부지가 대폭 감소되고, 제어부의 제어구조가 간단하여 고장발생율이 대폭 감소되는 것이다.Therefore, according to the present invention, it is possible to treat sewage / wastewater with a single reactor, and the control unit only needs to control the operation of the blower and the valve, thereby greatly reducing the installation cost and the required site, and simplifying the control structure of the control unit, resulting in failure rate. It is greatly reduced.

상술한 바와 같은 본 발명에 따른 하/폐수 처리 시스템에 의하면 단일 반응조로 하/폐수의 처리가 가능하게 되고 제어부가 블로워 및 밸브의 동작만 제어하면 되는 것이므로 설치비용 및 소요부지가 대폭 감소되고, 제어부의 제어구조가 간단하여 고장발생율이 대폭 감소되는 효과가 있으며, 복수개의 반응조를 병렬로 설치하여 교번동작시킴으로써 휴지기간없이 폐수를 처리할 수 있게 되는 효과가 있다.According to the sewage / wastewater treatment system according to the present invention as described above, it is possible to treat sewage / wastewater with a single reactor and the control unit only needs to control the operation of the blower and the valve, thereby greatly reducing the installation cost and the required site, and The simple structure of the control structure has the effect of greatly reducing the failure rate, and by installing a plurality of reactors in parallel, it is possible to treat wastewater without rest periods.

Claims (1)

유입되는 폐수에서 큰 부유물을 제거하는 스크린조(200)를 포함하는 하/폐수 처리 시스템에 있어서,In the sewage / wastewater treatment system comprising a screen tank 200 for removing a large float from the incoming wastewater, 폐수 유입구(212)가 상부 종단 인접부에 형성되어 일측 하단부만 개방형성된 제 1 격실(214)과 상기 제 1 격실(214)과 연통되어 상부에 처리수 유출구(216)가 형성된 제 2 격실(218)로 구성되는 반응조(210)와, 상기 스크린조(200)와 폐수유입구(212)사이를 연결하고 중간에 관로의 개폐를 제어하는 전동밸브(222)가 설치된 폐수유입관(224)과, 상기 반응조(210)내에 설치되어 폐수의 수위를 검출하는 수위검출센서(226)와, 반응조(210)의 외부에 설치된 블로워(230)와, 중간에 유로의 개폐를 제어하는 전동밸브(242)가 설치되어 상기 제 1, 2격실(214)(218)의 하부와 블로워(230)를 연결하는 산기관(240)과, 중간에 유로의 개폐를 제어하는 전동밸브(252)가 설치되어 상기 제 1 격실(214)에 연통되도록 설치되는 공기배출관(250)과, 중간에 유로의 개폐를 제어하는 전동밸브(262)가 설치되어 블로워(230)와 상기 공기배출관(250)의 밸브(252)와 제 1격실(214)사이를 연결하는 가압공기관(260)으로 구성되어 병렬설치된 반응장치(265)(265a)와;The wastewater inlet 212 is formed at an upper end adjacent to the first compartment 214 having only one lower end portion opened, and the second compartment 218 communicating with the first compartment 214 and having a treated water outlet 216 thereon. Wastewater inlet pipe 224 is installed between the reaction tank 210 and the screen tank 200 and the wastewater inlet 212 and the electric valve 222 for controlling the opening and closing of the pipeline in the middle, and The water level detection sensor 226 installed in the reactor 210 to detect the water level of the waste water, a blower 230 provided outside the reactor 210, and an electric valve 242 for controlling the opening and closing of the flow path in the middle are installed. And the diffuser 240 connecting the lower portions of the first and second compartments 214 and 218 to the blower 230, and an electric valve 252 for controlling the opening and closing of the flow path in the middle of the first compartment. An air discharge pipe 250 is installed to communicate with (214), and an electric valve 262 for controlling the opening and closing of the flow path in the middle is provided A reactor 265 and 265a installed in parallel with a blower 230 and a pressurized air engine 260 connecting between the valve 252 and the first compartment 214 of the air discharge pipe 250; 상기 수위검출센서(226)로부터 출력되는 신호를 기준으로 하여 폐수유입관밸브(222)와 산기관밸브(242)와 공기배출관밸브(252)와 블로워(230)및 가압공기관밸브(262)의 동작을 제어하여, 반응조(210)내부로 폐수를 유입시킨 후 폭기와 침전 및 배출과정을 수행하고, 이때 병렬설치된 복수개의 반응장치(265)(265a)내에서 일측 반응장치(265)가 폐수유입과정을 진행하는 동안 다른 반응장치(265a)가 폭기와 침전 및 처리수 배출과정을 진행하도록 하되, 폐수유입관밸브(222)와 산기관 밸브(242)와 공기배출관밸브(252)를 열고 가압공기관밸브(262)를 닫고 블로워(230)를 동작시켜 폐수유입과정을 진행한 후, 폐수유입관밸브(222)를 닫고 블로워(230)를 동작시켜 폭기과정을 진행하며, 폭기과정수행후 블로워(230)를 정지시켜 침전과정을 수행하고, 침전과정 수행후 산기관밸브(242)와 공기배출관밸브(252)를 닫고 가압공기관밸브(262)를 열고 블로워(230)를 동작시켜 처리수 배출과정을 진행하는 제어부(270)로 구성되는 것을 특징으로 하는 하/폐수 처리 시스템.Operation of the waste water inlet pipe valve 222, the diffuser valve 242, the air discharge pipe valve 252, the blower 230, and the pressurized air valve 262 based on the signal output from the water level detection sensor 226. By controlling the flow, the wastewater is introduced into the reaction tank 210, and then aeration and precipitation and discharge processes are performed. At this time, one side reaction apparatus 265 is disposed in a plurality of reactors 265 and 265a installed in parallel. While the other reactor (265a) to proceed with the process of aeration, sedimentation and treatment water discharge, while opening the wastewater inlet pipe valve 222 and diffuser valve 242 and air discharge pipe valve 252 and pressurized air valve After closing 262 and operating the blower 230 to proceed with the wastewater inflow process, closing the wastewater inlet pipe valve 222 and operating the blower 230 to proceed the aeration process, and after performing the aeration process blower 230 To stop the precipitation process, and after the precipitation process, the diffuser valve (242 ) And the air discharge pipe valve 252, the pressurized air pipe valve 262 is opened and the blower 230 is operated by the control unit 270 to proceed with the treatment water discharge process, characterized in that the sewage / wastewater treatment system.
KR1019990007702A 1999-03-09 1999-03-09 System of processing sewage KR100307260B1 (en)

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