WO2011025183A2 - Integrated sewage reuse device - Google Patents

Integrated sewage reuse device Download PDF

Info

Publication number
WO2011025183A2
WO2011025183A2 PCT/KR2010/005501 KR2010005501W WO2011025183A2 WO 2011025183 A2 WO2011025183 A2 WO 2011025183A2 KR 2010005501 W KR2010005501 W KR 2010005501W WO 2011025183 A2 WO2011025183 A2 WO 2011025183A2
Authority
WO
WIPO (PCT)
Prior art keywords
sewage
electrocoagulation
filter
treated water
reactor
Prior art date
Application number
PCT/KR2010/005501
Other languages
French (fr)
Korean (ko)
Other versions
WO2011025183A3 (en
Inventor
김현호
이재창
Original Assignee
Kim Hyun Ho
Lee Jae Chang
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 Kim Hyun Ho, Lee Jae Chang filed Critical Kim Hyun Ho
Publication of WO2011025183A2 publication Critical patent/WO2011025183A2/en
Publication of WO2011025183A3 publication Critical patent/WO2011025183A3/en

Links

Images

Classifications

    • 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
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • 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
    • C02F1/008Control or steering systems not provided for elsewhere in subclass C02F
    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/463Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
    • 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
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • 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
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/76Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
    • 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
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/26Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles

Definitions

  • the present invention relates to a device for treating and recycling sewage in a multi-use facility, industry, sewage treatment plant, etc. More specifically, an electro-coagulation method for sewage discharged from a multi-use facility, industry, sewage treatment plant, etc.
  • the present invention relates to an integrated sewage recycling apparatus for purifying by using, and filtration and sterilization through a plurality of filtration and sterilization apparatuses so as to be reused by making them into water or industrial water.
  • the multi-use facilities such as residential shopping malls, passenger terminals, large-scale marts, hospitals, public institutions, highway rest areas, military units, and government offices provide the drinking water, drinking water pipes, or drinking water pipes. It is temporarily stored in the water tank and supplied to the digestive or living water pipe.
  • sewage reuse device that can save water and prevent environmental pollution by treating sewage discharged from multi-use facilities by recycling it to heavy water or industrial water.
  • Most of the sewage reuse devices that have been used are large and complex due to biological treatment or chemical treatment, and thus have a large installation area, high maintenance costs, and low treatment efficiency, making them difficult to apply to sewage reuse.
  • the conventional heavy water treatment device has a number of problems such as a high cost for recovery time or maintenance when the seasonal factors or other problems occur, and the treatment efficiency is significantly lowered for long time use because it is difficult to clean the reactor. There is a problem.
  • the present invention is to solve the above problems, the object of the present invention is made of a simple configuration is particularly suitable for applying to multi-use facilities, by using the electro-coagulation method is high processing efficiency and operating cost An integrated sewage recycling apparatus can be reduced.
  • the magnetic field generator for atomizing the sewage molecules supplied from the outside;
  • An electrocoagulation unit for purifying the sewage supplied through the magnetic field generator by electro-coagulation;
  • the electroaggregation unit includes: an electrocoagulation reactor for receiving sewage from the outside and purifying the sewage by electrocoagulation; A plurality of power supply blades installed in the electrocoagulation reactor and electrically connected to an external power source to receive power; A plurality of metal blades disposed between the power blades; It may be configured to include a microbubble diffuser installed in the lower portion of the electrocoagulation reactor to generate a fine bubble.
  • the blade is preferably formed with fine embossing on the surface in order to increase the surface area.
  • microbubble diffuser is made of a porous hollow tube formed with fine pores through which air is discharged.
  • the electrocoagulation unit may further comprise a reaction vessel washer for supplying washing water into the electrocoagulation reactor for washing the electrocoagulation reactor.
  • the magnetic field generator may be composed of a hollow tube-shaped body mounted on the inlet of the electrocoagulation unit, and a plurality of semi-cylindrical magnets with high-density special processing mounted on the upper and lower portions of the inner circumferential surface of the body. .
  • the sewage recycling apparatus of the present invention has one end connected to the treated water collecting tank and the other end connected to the outlet side of the filter to supply the treated water of the treated water collecting tank to the filter.
  • It may be configured to further include a compressed air supply unit for supplying compressed air for washing.
  • the sewage reuse device of the present invention by making the particles of the sewage flowing into the electrocoagulation unit through the magnetic field generator finer, the electrocoagulation action can be made more smoothly to improve the treatment efficiency, scale or pollutants
  • the electrocoagulation action can be made more smoothly to improve the treatment efficiency, scale or pollutants
  • the blade in the electrocoagulation reactor of the electrocoagulation unit has a special surface treatment in the form of fine embossing to increase the surface area, ion elution is more smoothly performed, and thus the electrocoagulation action is more active, thereby further improving the treatment efficiency.
  • operating costs can be significantly reduced by minimizing power costs.
  • sewage reuse device is configured to continuously react and filter without having a separate treatment tank or filtration tank for biological treatment or chemical treatment. Therefore, a large installation area such as a conventional wastewater treatment apparatus is not required, and various components may be packaged to implement a compact and integrated sewage recycling apparatus.
  • sewage reuse device of the present invention can be advantageously applied not only to facilities such as industrial or sewage treatment plants, but also to multi-use facilities with a narrow or limited installation area.
  • FIG. 1 is a block diagram schematically showing the configuration of an integrated sewage recycling apparatus according to an embodiment of the present invention.
  • FIG. 2 is a block diagram illustrating a process of treating sewage water in the sewage recycling apparatus of FIG. 1.
  • FIG. 3 is a block diagram illustrating a process of washing the filter in the sewage recycling apparatus of FIG.
  • FIG. 4 is a cross-sectional view illustrating main parts of the magnetic field generator of the sewage recycling apparatus of FIG. 1.
  • FIG. 7 is a perspective view illustrating a magnet of the magnetic generating device of FIG. 4.
  • FIG. 6 is a cross-sectional view schematically illustrating main parts of an internal structure of an electrocoagulation reactor of the sewage recycling apparatus of FIG. 1.
  • FIG. 7 is a cross-sectional view schematically illustrating another example of the internal structure of the electrocoagulation reactor of the sewage recycling apparatus of FIG. 1.
  • FIG. 8 is a front view showing an embodiment of the blade of the sewage reuse device of FIG.
  • the integrated sewage recycling apparatus of the present invention includes a front end portion mainly composed of an electroaggregation unit for treating water sewage by electrocoagulation. It is composed of the rear end composed of the main shaft filtration device for various sites.
  • the sewage recycling apparatus of the present invention removes primary sewage from the sewage tank 10 through which the sewage is collected and the sewage pumped through the supply pipe 91 connected to the sewage tank 10.
  • a screen 20 a magnetic field generator 30 for atomizing the sewage molecules passing through the screen 20, an electrocoagulation unit 40 for treating the sewage by electro-coagulation, and The primary filter 50 and the secondary filter 60 to sequentially filter the treated water from the electrocoagulation unit 40, and the ozone generator to sterilize and remove untreated residual contaminants of the filtered water.
  • a chlorine injector 72 for injecting chlorine into the treated water
  • a treated water collecting tank 80 for storing the treated water
  • a controller (not shown) for controlling the overall operation of the sewage recycling apparatus.
  • the sewage collection tank 10 is connected to a pH adjuster 11 for adjusting the acidity.
  • the sewage collection tank 10 is equipped with a pH sensor and a flow meter.
  • the screen 20 is installed on the outlet of the sewage collection tank 10 or on the conduit of the supply pipe 91 connecting the sewage collection tank 10 and the electrocoagulation unit 40, from the sewage collection tank 10 to the electrocoagulation unit.
  • the large lumps of contaminants are primarily filtered from the sewage pumped to (40).
  • the magnetic field generator 30 has a hollow tube-shaped body 31 mounted to an inlet of the electrocoagulation reactor 41 of the electrocoagulation unit 40, and the body ( It consists of a magnet 32 mounted around the periphery 31.
  • the magnet 32 is specially processed to have a high density of magnetic force, made of a semi-cylindrical and attached to the upper and lower inner peripheral surfaces of the body 31, respectively.
  • the magnet 32 of the magnetic field generator 30 functions to make the molecular structure of sewage particles fine to improve the dissolving power and cleaning power of contaminants, and to keep the inside of the pipe clean by suppressing rust, water moss, and scale of the pipe. Do it.
  • the electrocoagulation unit 40 receives sewage from the sewage collection tank 10, an electrocoagulation reactor 41 for purifying sewage by electrocoagulation, and the electrocoagulation reactor 41.
  • the microbubble diffuser 42 is installed at the lower end of the interior to generate fine bubbles, and the reaction tank washer 43 for providing washing water into the electrocoagulation reactor 41 for cleaning the electrocoagulation reactor 41. do.
  • the electrocoagulation unit 40 includes a DC power supply 47 for supplying DC power to the blade 44 (see FIG. 6) for power in the electrocoagulation reactor 41.
  • a sensor (not shown) for measuring the voltage of the blade 44 for the power supply is installed inside the electrocoagulation reactor 41, and when the voltage between the blades 44 for the power becomes a set voltage, for example, 3V or less, the blade Replace 45 or wash the interior of the electrocoagulation reactor 41 is performed.
  • the electrocoagulation reactor 41 is preferably installed in one or more in parallel to minimize the installation area.
  • the electrocoagulation reactor 41 is disposed between the plurality of power blades 44 connected to an external DC power source and the power blade 44 to generate an electrochemical reaction.
  • the plurality of blades 45 are arranged vertically or horizontally.
  • the power blade 44 is preferably made of an insoluble metal such as stainless steel so that it can be used semi-permanently with little replacement.
  • the power supply blades 44 disposed at both ends of the power supply blades 44 are connected to the electrodes of the DC power supply 47, and are periodically supplied with power while their polarities are changed.
  • the power blades 44 disposed at both ends of the electrocoagulation reactor 41 are connected to the DC power supply 47 to form a single chamber structure.
  • the power blades 44 according to the degree of pollution of the sewage.
  • the electrode arrangement connected to the) may be divided into a plurality of chamber structure in one reactor to perform the electrocoagulation action.
  • the power blades 44 at both ends of the electrocoagulation reactor 41 and the power blades 44 in the center are connected to the DC power supply 47 to form the inside of the electrocoagulation reactor 41. May be divided into two chamber structures.
  • the blades 45 are made of a soluble metal such as iron or aluminum from which ions are eluted, and the surface is specially treated to increase the surface area, thereby forming fine embossings. have.
  • the hole 46 is preferably formed at the center of the upper end of the blade 45 so that the blade 45 can be easily detached from the electrocoagulation reactor 41.
  • the microbubble diffuser 42 generates fine bubbles in the lower portion of the electrocoagulation reactor 41 to facilitate the removal of contaminants of sewage and flotation of sedimentary flocculate in the electrocoagulation reactor 41 and the blades 45. To prevent the scale from adsorbing and remove some of the contaminants.
  • the microbubble diffuser 42 is connected to an external air supply 97 to receive compressed air, and is made of a porous hollow tube made of a material such as ceramic having ultra-fine pores formed on a surface thereof.
  • the air supplier 97 may be configured using, for example, an air compressor or a blower, an air pump, or the like.
  • the reaction vessel washer 43 of the electroaggregation unit 40 performs the electroaggregation process in the electroaggregation reactor 41 according to the characteristics of the contaminants for a predetermined time, and then performs the electroaggregation reactor 41. Supplying the washing water to the inside, and after a certain period of time by washing or discharged the washing water is completed through the sewage pipe to act to wash the electrocoagulation reactor (41).
  • the primary filter 50 and the secondary filter 60 filter the treated water treated in the electrocoagulation reactor 41 to filter the contaminants contained in the treated water.
  • the primary filter 50 may be configured using a carbon, a sand filter, or a mixed filter, but is not limited thereto.
  • the secondary filter 60 may be configured using a micro filter, but is not limited thereto.
  • the primary filter 50 may be configured in plural (two) in parallel, but alternatively may be configured in a single.
  • the primary filter 50 and the secondary filter 60 is connected to the air supply 97 for washing and is supplied with compressed air, and the treated water collection tank through the backwashing pipe 92 80) to supply water for cleaning.
  • the backwashing pipe 92 is provided with a third pump 96 for pumping water from the treated water collecting tank 80 to the primary filter and the secondary filter 50, 60.
  • the water which has been washed in the primary filter and the secondary filter (50, 60) is discharged to the sewage pipe through the drain pipe (93).
  • the ozone generator 71 treats untreated contaminants and sterilizes by injecting ozone into a supply pipe 91 connected to the treated water collecting tank 80.
  • the ozone generator 71 is preferably configured to be able to adjust the concentration according to the flow rate.
  • the chlorine injector 72 is connected to the supply pipe 91 connected to the treated water collection tank 80 to inject a predetermined amount of chlorine, and like the ozone generator 71 to adjust the concentration of chlorine according to the flow rate. It is preferred to have a flow meter and a metering pump.
  • the controller integrally controls all components of the sewage reuse device, and is configured to enable real-time monitoring, feedback control, and remote control.
  • reference numeral 94 denotes a first pump for pumping sewage from the sewage collecting tank 10 to the electrocoagulation unit 40
  • reference numeral 95 is an electrocoagulation unit 40 to the primary filter 50. It is a 2nd pump which feeds process water.
  • reference numerals V1 to V15 are valves for controlling the flow of sewage or treated water through respective pipes, and the valves may use a well-known valve such as an electric valve or a pneumatic valve.
  • the pneumatic valve is preferably configured to be connected to the air supply 97 to receive the pneumatic pressure.
  • the sewage reuse device configured as above operates as follows.
  • FIG. 2 is a view showing a process of water treatment of sewage, when the sewage is stored in the sewage collection tank 10 at a certain level, the first pump 94 is operated to adjust the pH (pH) of the sewage collection tank 10 Sewage flows through the supply pipe (91). At this time, the sewage is filtered through the screen 20 while the primary contaminants are filtered out, and the sewage molecules are granulated by the magnetic field generator 30.
  • the sewage that has passed through the magnetic field generator 30 is introduced into the electrocoagulation reactor 41 through an inlet port under the electrocoagulation reactor 41.
  • the power is applied to the blade 44 for power in the electrocoagulation reactor 41, the sewage is electrolyzed, and the metal ions eluted from the electrode destabilize the particles stably present and at the same time floc to remove contaminants. And flocculate harmful substances by electrical oxidation and reduction.
  • the compressed air is supplied from the air supplier 97 to the microbubble diffuser 42 while the electrocoagulation action is performed in the electrocoagulation reactor 41, and ultra-bubbles are released from the microbubble diffuser 42.
  • the microbubbles released from the microbubble diffuser 42 facilitate the removal of contaminants of sewage and flotation of sedimentary flocculate in the electrocoagulation reactor 41 to prevent the scale from adsorbing to the blade 45. do.
  • the treated water purified by the electrocoagulation reactor 41 is sequentially introduced into the primary filter 50 and the secondary filter 60 by the second pump 95 to filter out residual condensate and contaminants that have not been contaminated.
  • the treated water passing through the secondary filter 60 is sent to the treated water collecting tank 80 through the supply pipe 91, in which a certain amount of ozone is injected by the ozone generator 71 to perform sterilization. In addition, a certain amount of chlorine is injected through the chlorine injector 72.
  • the treated water treated through the above process is stored in the treated water collecting tank 80 and then reused as reused water for heavy water or other uses.
  • the treated water supplied to the primary filter 50 and / or the secondary filter 60 flows in from the outlet side of the primary filter 50 and / or the secondary filter 60 so that the primary filter 50 and / or The washing is performed while the secondary filter 60 is flowed upside down and then discharged to the sewer pipe through a drain pipe 93 connected to the inlet side of the primary filter 50 and / or the secondary filter 60.
  • the electroagglomeration reactor 41 of the electrocoagulation unit 40 is also periodically required to clean, first discharge the sewage in the electrocoagulation reactor 41 to the outside to empty the inside of the electrocoagulation reactor 41, the reaction vessel washer Supply wash water from (43) and fill up to the set level.
  • the washing is discharged to the outside or recovered again to the reaction vessel washer 43, the washing is completed.
  • the sewage recycling apparatus of the present invention has an advantage that the electrocoagulation action can be made more smoothly by making particles of sewage flowing into the electrocoagulation unit 40 through a magnetic field generator, thereby improving treatment efficiency. .
  • the surface of the blade 45 in the electrocoagulation reactor 41 has a special surface treatment, fine embossing is formed to increase the surface area, ion elution is more smoothly performed, and thus the electrocoagulation action becomes more active, thereby improving treatment efficiency. It can be further improved, and power consumption can be reduced.
  • the electroaggregation reactor 41 of the electroaggregation unit 40 is configured as one, but alternatively, the electroaggregation reactor 41 may be configured in plural in parallel.
  • the present invention can be applied to a sewage reuse device or a sewage treatment device for purifying sewage discharged from a multi-use facility, an industry, a sewage treatment plant and the like.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The present invention relates to an integrated sewage reuse device which is applicable to multi-purpose facilities or industries and sewage disposal plants, realizes a high processing efficiency by using the electro-coagulation method, and reduces driving costs. According to the present invention, the sewage reuse device comprises: a sewage tank (10) in which sewage is collected; a screen (20) which eliminates primary concomitants of the sewage transferred through a feeding line (91) that is connected to the sewage tank (10); a magnetic field generator (30) which atomizes molecules of the sewage that has passed through the screen (20); an electro-coagulation unit (40) which purifies the sewage by the electro-coagulation method; primary filters (50) and a secondary filter (60) which sequentially filter the wastewater purified in the electro-coagulation unit (40); an ozone generator (71) which sterilizes and eliminates the residual contaminants that have not been treated from the filtered wastewater; a chlorine injector (72) which injects chlorine into the wastewater; a wastewater tank (80) which stores the wastewater; and a controller which controls the overall operation of the sewage reuse device.

Description

일체형 하수 재이용 장치Integrated sewage reuse device
본 발명은 다중 이용시설이나 산업체, 하수처리장 등의 하수를 처리하여 재활용하는 장치에 관한 것으로, 더욱 상세하게는 다중 이용시설이나 산업체, 하수처리장 등에서 방류되는 하수를 전기응집(electro-coagulation) 방식을 이용하여 정화시키고, 복수의 여과 및 살균 장치를 통해 여과 및 살균시켜 중수도나 공업용수로 만들어 재이용할 수 있도록 하는 일체형 하수 재이용 장치에 관한 것이다. The present invention relates to a device for treating and recycling sewage in a multi-use facility, industry, sewage treatment plant, etc. More specifically, an electro-coagulation method for sewage discharged from a multi-use facility, industry, sewage treatment plant, etc. The present invention relates to an integrated sewage recycling apparatus for purifying by using, and filtration and sterilization through a plurality of filtration and sterilization apparatuses so as to be reused by making them into water or industrial water.
일반적으로, 주상복합상가, 여객터미널, 대형마트, 병원, 공공기관, 고속도로 휴게소, 군부대, 관공서 등의 다중 이용시설의 소화관이나 생활용수관, 음용수관은 시수인입관을 통해 시수가 공급되거나, 시수가 물탱크에 임시 저장되었다가 소화관이나 생활용수관 등으로 공급되도록 되어 있다.In general, the multi-use facilities such as residential shopping malls, passenger terminals, large-scale marts, hospitals, public institutions, highway rest areas, military units, and government offices provide the drinking water, drinking water pipes, or drinking water pipes. It is temporarily stored in the water tank and supplied to the digestive or living water pipe.
종래에는 시수가 중단되면, 소화시설은 물론 생활용수나 음용수를 물탱크에 저장된 물에 의존할 수 밖에 없어, 생활용수가 부족하게 됨은 물론, 화재발생에 무방비상태가 되는 문제점이 있었다. In the related art, when the water is stopped, there is a problem in that not only the fire extinguishing facility but also the living water and drinking water are dependent on the water stored in the water tank, and thus the living water is insufficient and becomes defenseless against fire.
또한, 시수만을 공급원으로 하고 일회 사용으로 버려지게 되므로, 물이 낭비되어 경제적이지 못했고 환경오염에도 악영향을 미치는 문제점이 있었다.In addition, since only the water is used as a source and discarded in one-time use, water was not used because it was not economical and there was a problem that adversely affects environmental pollution.
이러한 문제를 해결하기 위하여 다중 이용시설에서 배출되는 하수를 정수처리하여 중수도나 공업용수 등으로 재활용함으로써 물을 절약하고 환경오염을 방지할 수 있는 하수 재이용 장치의 개발이 절실히 요구되고 있으나, 현재까지 개발된 하수 재이용 장치의 대부분은 생물학적 처리나 약품 처리 등으로 크고 복잡하여 설치면적이 넓고, 유지 관리 비용이 많이 소요되며, 처리 효율이 낮아 하수 재이용에 적용하기 어려운 문제가 있었다. In order to solve this problem, it is urgently needed to develop a sewage reuse device that can save water and prevent environmental pollution by treating sewage discharged from multi-use facilities by recycling it to heavy water or industrial water. Most of the sewage reuse devices that have been used are large and complex due to biological treatment or chemical treatment, and thus have a large installation area, high maintenance costs, and low treatment efficiency, making them difficult to apply to sewage reuse.
또한, 종래의 중수처리장치는 계절적 요인이나 기타 운전에 문제가 발생하면 복구시간이나 보수유지에 고비용이 지출되는 등 많은 문제점을 가지고 있으며, 반응조의 세척이 어렵기 때문에 장시간 사용시 처리 효율이 현저하게 저하되는 문제가 있다. In addition, the conventional heavy water treatment device has a number of problems such as a high cost for recovery time or maintenance when the seasonal factors or other problems occur, and the treatment efficiency is significantly lowered for long time use because it is difficult to clean the reactor. There is a problem.
본 발명은 상기와 같은 문제를 해결하기 위한 것으로, 본 발명의 목적은 간단한 구성으로 이루어져 특히 다중 이용시설에 적용하기 적합하며, 전기응집(electro-coagulation)방식을 이용하여 처리 효율이 높고 운전 비용을 줄일 수 있는 일체형 하수 재이용 장치를 제공함에 있다. The present invention is to solve the above problems, the object of the present invention is made of a simple configuration is particularly suitable for applying to multi-use facilities, by using the electro-coagulation method is high processing efficiency and operating cost An integrated sewage recycling apparatus can be reduced.
상기와 같은 목적을 달성하기 위한 본 발명은, 외부에서 공급되는 하수의 분자를 미립자화시키는 자기장발생기와; 상기 자기장발생기를 통과하여 공급된 하수를 전기응집(electro-coagulation)에 의해 정수 처리하는 전기응집유닛과; 상기 전기응집유닛을 통해 정수 처리된 처리수에서 잔여 오염물을 걸러내는 여과기와; 상기 여과기를 통과한 처리수가 저장되는 처리수 집수조를 포함하여 구성된 것을 특징으로 하는 일체형 하수 재이용 장치를 제공한다.The present invention for achieving the above object, the magnetic field generator for atomizing the sewage molecules supplied from the outside; An electrocoagulation unit for purifying the sewage supplied through the magnetic field generator by electro-coagulation; A filter for filtering out residual contaminants from the purified water through the electrocoagulation unit; It provides an integrated sewage recycling apparatus comprising a treated water collecting tank for storing the treated water passing through the filter.
본 발명의 한 형태에 따르면, 상기 전기응집유닛은, 외부로부터 하수를 공급받아 전기응집에 의해 하수를 정수하는 전기응집 반응조와; 상기 전기응집 반응조의 내부에 설치되며, 외부의 전원과 전기적으로 연결되어 전원을 인가받는 복수개의 전원용 블레이드와; 상기 전원용 블레이드 사이에 배치되는 복수개의 금속재 블레이드와; 상기 전기응집 반응조 내부의 하부에 설치되어 미세한 기포를 생성하는 마이크로버블 산기관을 포함하여 구성될 수 있다. According to one aspect of the present invention, the electroaggregation unit includes: an electrocoagulation reactor for receiving sewage from the outside and purifying the sewage by electrocoagulation; A plurality of power supply blades installed in the electrocoagulation reactor and electrically connected to an external power source to receive power; A plurality of metal blades disposed between the power blades; It may be configured to include a microbubble diffuser installed in the lower portion of the electrocoagulation reactor to generate a fine bubble.
여기서, 상기 블레이드는 표면적을 증대시키기 위하여 표면에 미세한 엠보싱이 형성된 것이 바람직하다. Here, the blade is preferably formed with fine embossing on the surface in order to increase the surface area.
그리고, 상기 마이크로버블 산기관은 공기가 방출되는 미세한 기공이 형성된 다공성 중공관으로 이루어진다. In addition, the microbubble diffuser is made of a porous hollow tube formed with fine pores through which air is discharged.
본 발명의 다른 한 형태에 따르면, 상기 전기응집유닛은 상기 전기응집 반응조의 세척을 위해 전기응집 반응조 내부로 세척수를 공급하는 반응조세척기를 더 포함하여 구성될 수 있다. According to another aspect of the present invention, the electrocoagulation unit may further comprise a reaction vessel washer for supplying washing water into the electrocoagulation reactor for washing the electrocoagulation reactor.
그리고, 상기 자기장발생기는 상기 전기응집유닛의 유입구에 장착되는 중공관 형태의 몸체와, 상기 몸체의 내주면의 상부 및 하부 각각에 장착되는 고밀도로 특수가공처리된 복수개의 반원통형 마그네트로 구성될 수 있다. In addition, the magnetic field generator may be composed of a hollow tube-shaped body mounted on the inlet of the electrocoagulation unit, and a plurality of semi-cylindrical magnets with high-density special processing mounted on the upper and lower portions of the inner circumferential surface of the body. .
*본 발명의 또 다른 한 형태에 따르면, 본 발명의 하수 재이용 장치는 일단이 상기 처리수 집수조에 연결되고 타단이 상기 여과기의 배출구 쪽에 연결되어 처리수 집수조의 처리수를 여과기로 공급하는 역세용 배관과, 상기 역세용 배관을 통해 상기 여과기로 세척을 위한 처리수를 압송하는 펌프와, 상기 여과기의 유입구 쪽에 연결되어 여과기를 세척한 후 배출되는 처리수를 외부로 유도하는 드레인 배관 및, 상기 여과기에 세척을 위한 압축공기를 공급하는 압축공기 공급유닛을 더 포함하여 구성될 수 있다. According to yet another aspect of the present invention, the sewage recycling apparatus of the present invention has one end connected to the treated water collecting tank and the other end connected to the outlet side of the filter to supply the treated water of the treated water collecting tank to the filter. And a pump for pumping the treated water for washing to the strainer through the backwashing pipe, a drain pipe connected to the inlet side of the strainer to wash the strainer, and guide the treated water discharged to the outside, and to the strainer. It may be configured to further include a compressed air supply unit for supplying compressed air for washing.
이러한 본 발명에 따르면, 본 발명의 하수 재이용 장치는 자기장발생기를 통해 전기응집유닛으로 유입되는 하수의 분자를 미립자화시킴으로써 전기응집 작용이 더욱 원활하게 이루어져 처리 효율을 향상시킬 수 있고, 스케일이나 오염물질을 제거함은 물론 배관 녹과 때를 제거하여 유지관리가 용이한 이점이 있다. According to the present invention, the sewage reuse device of the present invention by making the particles of the sewage flowing into the electrocoagulation unit through the magnetic field generator finer, the electrocoagulation action can be made more smoothly to improve the treatment efficiency, scale or pollutants Of course, there is an advantage of easy maintenance by removing pipe rust and dirt.
그리고, 상기 전기응집유닛의 전기응집 반응조 내의 블레이드가 미세한 엠보싱 형태로 특수 표면처리되어 표면적이 증대되므로 이온 용출이 더욱 원활하게 이루어지고, 이에 따라 전기응집 작용이 더욱 활발해져 처리 효율을 더욱 향상시킬 수 있고, 전력비용을 최소화하여 운전비용을 획기적으로 줄일 수 있다. In addition, since the blade in the electrocoagulation reactor of the electrocoagulation unit has a special surface treatment in the form of fine embossing to increase the surface area, ion elution is more smoothly performed, and thus the electrocoagulation action is more active, thereby further improving the treatment efficiency. In addition, operating costs can be significantly reduced by minimizing power costs.
또한, 기존의 하수 재이용 장치와는 달리 생물학적 처리나 약품 처리를 위한별도의 처리조나 여과조를 두지 않고 연속적으로 반응하고 여과할 수 있도록 구성되어 있다. 따라서, 기존의 오폐수 처리장치와 같은 넓은 설치 면적이 필요치 않으며, 여러 구성부들을 패키지화시켜 콤팩트하고 일체화된 하수 재이용 장치를 구현할 수 있다. In addition, unlike the existing sewage reuse device is configured to continuously react and filter without having a separate treatment tank or filtration tank for biological treatment or chemical treatment. Therefore, a large installation area such as a conventional wastewater treatment apparatus is not required, and various components may be packaged to implement a compact and integrated sewage recycling apparatus.
상술한 것과 같은 본 발명의 이점들은 본 발명의 하수 재이용 장치를 산업체나 하수처리장과 같은 시설 뿐만 아니라, 설치 면적이 협소하거나 제한된 다중 이용시설에도 유리하게 적용할 수 있는 이점을 제공한다. Advantages of the present invention as described above provide the advantage that the sewage reuse device of the present invention can be advantageously applied not only to facilities such as industrial or sewage treatment plants, but also to multi-use facilities with a narrow or limited installation area.
도 1은 본 발명의 일 실시예에 따른 일체형 하수 재이용 장치의 구성을 개략적으로 나타낸 블록도이다. 1 is a block diagram schematically showing the configuration of an integrated sewage recycling apparatus according to an embodiment of the present invention.
도 2는 도 1의 하수 재이용 장치에서 하수가 정수 처리되는 과정을 나타낸 블록도이다. FIG. 2 is a block diagram illustrating a process of treating sewage water in the sewage recycling apparatus of FIG. 1.
도 3은 도 1의 하수 재이용 장치에서 여과기의 세척이 이루어지는 과정을 나타낸 블록도이다. 3 is a block diagram illustrating a process of washing the filter in the sewage recycling apparatus of FIG.
도 4는 도 1의 하수 재이용 장치의 자기장발생기의 구성을 개략적으로 나타낸 요부 단면도이다. 4 is a cross-sectional view illustrating main parts of the magnetic field generator of the sewage recycling apparatus of FIG. 1.
도 7는 도 4의 자기발생장치의 마그네트의 형태를 나타낸 사시도이다. FIG. 7 is a perspective view illustrating a magnet of the magnetic generating device of FIG. 4.
도 6은 도 1의 하수 재이용 장치의 전기응집 반응조의 내부 구조의 일 실시예를 개략적으로 나타낸 요부 단면도이다. 6 is a cross-sectional view schematically illustrating main parts of an internal structure of an electrocoagulation reactor of the sewage recycling apparatus of FIG. 1.
도 7은 도 1의 하수 재이용 장치의 전기응집 반응조의 내부 구조의 다른 실시예를 개략적으로 나타낸 요부 단면도이다. FIG. 7 is a cross-sectional view schematically illustrating another example of the internal structure of the electrocoagulation reactor of the sewage recycling apparatus of FIG. 1.
도 8은 도 1의 하수 재이용 장치의 블레이드의 일 실시예를 나타낸 정면도이다. 8 is a front view showing an embodiment of the blade of the sewage reuse device of FIG.
이하, 첨부된 도면을 참조하여 본 발명에 따른 일체형 하수 재이용 장치의 바람직한 실시예를 상세히 설명한다. Hereinafter, with reference to the accompanying drawings will be described in detail a preferred embodiment of the integrated sewage recycling apparatus according to the present invention.
도 1 내지 도 8은 본 발명의 일 실시예에 따른 일체형 하수 재이용 장치를 나타낸 것으로, 본 발명의 일체형 하수 재이용 장치는 전기응집 작용에 의해 하수를 정수 처리하는 전기응집유닛을 메인으로 하는 전단부와 각종 현장에 맞는 여과장치를 주축으로 구성된 후단부로 이루어진다.1 to 8 illustrate an integrated sewage recycling apparatus according to an embodiment of the present invention, the integrated sewage recycling apparatus of the present invention includes a front end portion mainly composed of an electroaggregation unit for treating water sewage by electrocoagulation. It is composed of the rear end composed of the main shaft filtration device for various sites.
먼저 도 1을 참조하면, 본 발명의 하수 재이용 장치는 하수가 집수되는 하수 집수조(10)와, 상기 하수 집수조(10)에 연결된 공급배관(91)을 통해 압송되는 하수의 1차 협잡물을 제거하는 스크린(20)과, 상기 스크린(20)을 통과한 하수의 분자를 미립자화하는 자기장발생기(30)와, 전기응집(electro-coagulation)에 의해 하수를 정수처리하는 전기응집유닛(40)과, 상기 전기응집유닛(40)에서 정수 처리된 처리수를 차례로 여과시키는 1차 여과기(50) 및 2차 여과기(60)와, 상기 여과 처리된 처리수의 미처리된 잔여 오염물을 살균 및 제거하는 오존발생기(71)와, 처리수에 염소를 주입하는 염소주입기(72) 및, 처리수를 저장하는 처리수 집수조(80) 및, 하수 재이용 장치의 전체 작동을 제어하는 컨트롤러(미도시)로 구성된다. First, referring to FIG. 1, the sewage recycling apparatus of the present invention removes primary sewage from the sewage tank 10 through which the sewage is collected and the sewage pumped through the supply pipe 91 connected to the sewage tank 10. A screen 20, a magnetic field generator 30 for atomizing the sewage molecules passing through the screen 20, an electrocoagulation unit 40 for treating the sewage by electro-coagulation, and The primary filter 50 and the secondary filter 60 to sequentially filter the treated water from the electrocoagulation unit 40, and the ozone generator to sterilize and remove untreated residual contaminants of the filtered water. 71, a chlorine injector 72 for injecting chlorine into the treated water, a treated water collecting tank 80 for storing the treated water, and a controller (not shown) for controlling the overall operation of the sewage recycling apparatus.
상기 하수 집수조(10)에는 산도를 조정하는 pH조정기(11)가 연결되어 있다. 그리고, 상기 하수 집수조(10)에 pH센서 및 유량계 등이 장착되어 있다. The sewage collection tank 10 is connected to a pH adjuster 11 for adjusting the acidity. The sewage collection tank 10 is equipped with a pH sensor and a flow meter.
상기 스크린(20)은 하수 집수조(10)의 배출구 또는 하수 집수조(10)와 전기응집유닛(40)을 연결하는 공급배관(91)의 관로 상에 설치되어, 하수 집수조(10)로부터 전기응집유닛(40)으로 압송되는 하수에서 덩어리가 큰 오염물을 1차적으로 걸러낸다. The screen 20 is installed on the outlet of the sewage collection tank 10 or on the conduit of the supply pipe 91 connecting the sewage collection tank 10 and the electrocoagulation unit 40, from the sewage collection tank 10 to the electrocoagulation unit. The large lumps of contaminants are primarily filtered from the sewage pumped to (40).
상기 자기장발생기(30)는 도 4 및 도 5에 도시된 것과 같이, 상기 전기응집유닛(40)의 전기응집 반응조(41)의 유입구에 장착되는 중공관 형태의 몸체(31)와, 상기 몸체(31)의 둘레에 장착되는 마그네트(32)로 이루어진다. 이 실시예에서 상기 마그네트(32)는 특수가공처리되어 고밀도의 자력을 가지며, 반원통형으로 이루어져 상기 몸체(31)의 내주면 상부 및 하부 각각에 부착된다. 상기 자기장발생기(30)의 마그네트(32)는 하수의 분자구조를 미립자화시켜 오염물의 용해력과 세정력을 향상시키고, 배관의 녹이나 물이끼, 스케일(scale) 등을 억제하여 배관 내부를 깨끗하게 유지시키는 기능을 한다. As shown in FIGS. 4 and 5, the magnetic field generator 30 has a hollow tube-shaped body 31 mounted to an inlet of the electrocoagulation reactor 41 of the electrocoagulation unit 40, and the body ( It consists of a magnet 32 mounted around the periphery 31. In this embodiment, the magnet 32 is specially processed to have a high density of magnetic force, made of a semi-cylindrical and attached to the upper and lower inner peripheral surfaces of the body 31, respectively. The magnet 32 of the magnetic field generator 30 functions to make the molecular structure of sewage particles fine to improve the dissolving power and cleaning power of contaminants, and to keep the inside of the pipe clean by suppressing rust, water moss, and scale of the pipe. Do it.
다시, 도 1을 참조하면, 상기 전기응집유닛(40)은 상기 하수 집수조(10)로부터 하수를 공급받아 전기응집에 의해 하수를 정수하는 전기응집 반응조(41)와, 상기 전기응집 반응조(41) 내부의 하단부에 설치되어 미세한 기포를 생성하는 마이크로버블 산기관(42)과, 상기 전기응집 반응조(41)의 세척을 위해 전기응집 반응조(41) 내부로 세척수를 제공하는 반응조세척기(43)를 포함한다. 도면에 도시하지는 않았으나, 상기 전기응집유닛(40)은 상기 전기응집 반응조(41) 내의 전원용 블레이드(44)(도 6참조)에 직류 전원을 공급하기 위한 DC전원공급부(47)가 구성된다. 그리고, 전기응집 반응조(41) 내부에는 전원용 블레이드(44)의 전압을 측정하는 센서(미도시)가 설치되어, 전원용 블레이드(44) 간의 전압이 설정 전압, 예를 들어 3V 이하가 될 경우에는 블레이드(45)를 교체하거나 전기응집 반응조(41) 내부를 세척하는 공정이 수행된다. Again, referring to FIG. 1, the electrocoagulation unit 40 receives sewage from the sewage collection tank 10, an electrocoagulation reactor 41 for purifying sewage by electrocoagulation, and the electrocoagulation reactor 41. The microbubble diffuser 42 is installed at the lower end of the interior to generate fine bubbles, and the reaction tank washer 43 for providing washing water into the electrocoagulation reactor 41 for cleaning the electrocoagulation reactor 41. do. Although not shown in the figure, the electrocoagulation unit 40 includes a DC power supply 47 for supplying DC power to the blade 44 (see FIG. 6) for power in the electrocoagulation reactor 41. In addition, a sensor (not shown) for measuring the voltage of the blade 44 for the power supply is installed inside the electrocoagulation reactor 41, and when the voltage between the blades 44 for the power becomes a set voltage, for example, 3V or less, the blade Replace 45 or wash the interior of the electrocoagulation reactor 41 is performed.
상기 전기응집 반응조(41)는 한개 또는 다수를 병렬로 설치하여 설치면적을 최소화하는 것이 바람직하다. The electrocoagulation reactor 41 is preferably installed in one or more in parallel to minimize the installation area.
도 6에 도시된 것과 같이, 상기 전기응집 반응조(41)의 내부에는 외부의 직류전원과 연결되는 복수개의 전원용 블레이드(44)들과, 상기 전원용 블레이드(44) 사이에 배치되어 전기화학 반응을 일으키는 복수개의 블레이드(45)들이 수직 또는 수평하게 배치된다. 상기 전원용 블레이드(44)는 교체가 거의 필요없이 반영구적으로 사용 가능하도록 스테인레스스틸 등의 불용성 금속으로 만들어지는 것이 바람직하다. 상기 전원용 블레이드(44)들중 양단부에 배치된 전원용 블레이드(44)들은 상기 DC전원공급부(47)의 전극과 연결되며, 주기적으로 극성이 전환되면서 전원을 인가받는다. As shown in FIG. 6, the electrocoagulation reactor 41 is disposed between the plurality of power blades 44 connected to an external DC power source and the power blade 44 to generate an electrochemical reaction. The plurality of blades 45 are arranged vertically or horizontally. The power blade 44 is preferably made of an insoluble metal such as stainless steel so that it can be used semi-permanently with little replacement. The power supply blades 44 disposed at both ends of the power supply blades 44 are connected to the electrodes of the DC power supply 47, and are periodically supplied with power while their polarities are changed.
이 실시예에서는 상기 전기응집 반응조(41)의 양단에 배치된 전원용 블레이드(44)가 DC전원공급부(47)와 연결되어 단일 챔버 구조를 이루지만, 이와 다르게 하수의 오염 정도에 따라 전원용 블레이드(44)에 연결되는 전극 배열을 달리하여 한 개의 반응조 내에서 복수 챔버 구조로 분할하여 전기응집 작용을 수행할 수도 있을 것이다. In this embodiment, the power blades 44 disposed at both ends of the electrocoagulation reactor 41 are connected to the DC power supply 47 to form a single chamber structure. Alternatively, the power blades 44 according to the degree of pollution of the sewage. By varying the electrode arrangement connected to the) may be divided into a plurality of chamber structure in one reactor to perform the electrocoagulation action.
예를 들어, 도 7에 도시한 것과 같이, 전기응집 반응조(41) 양단부의 전원용 블레이드(44)와 가운데의 전원용 블레이드(44)를 DC전원공급부(47)에 연결하여 전기응집 반응조(41) 내부를 2 챔버 구조로 분할할 수도 있을 것이다. For example, as illustrated in FIG. 7, the power blades 44 at both ends of the electrocoagulation reactor 41 and the power blades 44 in the center are connected to the DC power supply 47 to form the inside of the electrocoagulation reactor 41. May be divided into two chamber structures.
한편, 도 6 및 도 8에 도시된 것과 같이, 상기 블레이드(45)들은 이온이 용출되는 철 또는 알루미늄 등의 가용성 금속으로 만들어지며, 표면적을 증대시키기 위해 표면이 특수표면처리되어 미세한 엠보싱들이 형성되어 있다. 또한, 상기 블레이드(45)들의 상단부 중앙에는 블레이드(45)를 전기응집 반응조(41)에 용이하게 탈착시킬 수 있도록 홀(46)이 형성됨이 바람직하다. 6 and 8, the blades 45 are made of a soluble metal such as iron or aluminum from which ions are eluted, and the surface is specially treated to increase the surface area, thereby forming fine embossings. have. In addition, the hole 46 is preferably formed at the center of the upper end of the blade 45 so that the blade 45 can be easily detached from the electrocoagulation reactor 41.
상기 마이크로버블 산기관(42)은 전기응집 반응조(41) 내의 하부에서 미세한 기포를 생성하여 전기응집 반응조(41) 내의 하수의 오염물 제거와 침전성 응집물(flocculate)의 부상을 원활하게 하여 블레이드(45)에 스케일이 흡착되는 것을 방지하고 오염물의 일부를 제거한다. 상기 마이크로버블 산기관(42)은 외부의 공기공급기(97)와 연결되어 압축공기를 공급받으며, 표면에 초미세 기공이 형성된 세라믹 등의 재질로 된 다공성 중공관으로 이루어진다. 상기 공기공급기(97)는 예컨대 공기압축기(air compressor) 또는 송풍기, 공기펌프 등을 이용하여 구성될 수 있다. The microbubble diffuser 42 generates fine bubbles in the lower portion of the electrocoagulation reactor 41 to facilitate the removal of contaminants of sewage and flotation of sedimentary flocculate in the electrocoagulation reactor 41 and the blades 45. To prevent the scale from adsorbing and remove some of the contaminants. The microbubble diffuser 42 is connected to an external air supply 97 to receive compressed air, and is made of a porous hollow tube made of a material such as ceramic having ultra-fine pores formed on a surface thereof. The air supplier 97 may be configured using, for example, an air compressor or a blower, an air pump, or the like.
다시 도 1을 참조하면, 상기 전기응집유닛(40)의 반응조세척기(43)는 오염물의 특성에 따라 전기응집 반응조(41)에서의 전기응집 처리를 일정 시간 수행한 후 상기 전기응집 반응조(41) 내부에 세척수를 공급하고, 일정 시간 경과 후 세척이 완료되는 세척수를 회수 또는 하수관거를 통해 방류함으로써 전기응집 반응조(41)를 세척하는 작용을 한다. Referring back to FIG. 1, the reaction vessel washer 43 of the electroaggregation unit 40 performs the electroaggregation process in the electroaggregation reactor 41 according to the characteristics of the contaminants for a predetermined time, and then performs the electroaggregation reactor 41. Supplying the washing water to the inside, and after a certain period of time by washing or discharged the washing water is completed through the sewage pipe to act to wash the electrocoagulation reactor (41).
상기 1차 여과기(50)와 2차 여과기(60)는 전기응집 반응조(41)에서 처리된 처리수를 여과하여 처리수에 포함된 오염물을 걸러낸다. 상기 1차 여과기(50)는 카본이나 샌드필터 또는 혼합형태의 필터 등을 이용하여 구성할 수 있으나, 그 종류에 제한을 두지는 않는다. 또한, 상기 2차 여과기(60)는 마이크로필터 등을 이용하여 구성할 수 있으나, 역시 그 종류에 제한을 두지는 않는다. 이 실시예에서 상기 1차 여과기(50)는 복수개(2개)가 병렬로 구성되나, 이와 다르게 단일하게 구성될 수도 있다. The primary filter 50 and the secondary filter 60 filter the treated water treated in the electrocoagulation reactor 41 to filter the contaminants contained in the treated water. The primary filter 50 may be configured using a carbon, a sand filter, or a mixed filter, but is not limited thereto. In addition, the secondary filter 60 may be configured using a micro filter, but is not limited thereto. In this embodiment, the primary filter 50 may be configured in plural (two) in parallel, but alternatively may be configured in a single.
또한, 상기 1차 여과기(50)와 2차 여과기(60)는 세척을 위해 상기 공기공급기(97)와 연결되어 압축공기를 공급받음과 더불어, 역세용 배관(92)을 통해 상기 처리수 집수조(80)와 연결되어 세척을 위한 물을 공급받는다. 상기 역세용 배관(92)에는 처리수 집수조(80)의 물을 1차 여과기 및 2차 여과기(50, 60)로 압송하기 위한 제3펌프(96)가 설치된다. 상기 1차 여과기 및 2차 여과기(50, 60)에서 세척이 완료된 물은 드레인 배관(93)을 통해 하수관거로 배출된다. In addition, the primary filter 50 and the secondary filter 60 is connected to the air supply 97 for washing and is supplied with compressed air, and the treated water collection tank through the backwashing pipe 92 80) to supply water for cleaning. The backwashing pipe 92 is provided with a third pump 96 for pumping water from the treated water collecting tank 80 to the primary filter and the secondary filter 50, 60. The water which has been washed in the primary filter and the secondary filter (50, 60) is discharged to the sewage pipe through the drain pipe (93).
상기 오존발생기(71)는 상기 처리수 집수조(80)로 연결되는 공급배관(91)에 오존을 일정량 주입함으로써 미처리된 오염물을 처리하고 살균 처리를 한다. 상기 오존발생기(71)는 유량에 따른 농도 조절이 가능하게 구성됨이 바람직하다. The ozone generator 71 treats untreated contaminants and sterilizes by injecting ozone into a supply pipe 91 connected to the treated water collecting tank 80. The ozone generator 71 is preferably configured to be able to adjust the concentration according to the flow rate.
그리고, 상기 염소주입기(72)는 처리수 집수조(80)로 연결되는 공급배관(91)에 연결되어 일정량의 염소를 주입하며, 오존발생기(71)와 마찬가지로 유량에 따른 염소의 농도를 조절할 수 있도록 유량계 및 정량펌프를 구비함이 바람직하다. In addition, the chlorine injector 72 is connected to the supply pipe 91 connected to the treated water collection tank 80 to inject a predetermined amount of chlorine, and like the ozone generator 71 to adjust the concentration of chlorine according to the flow rate. It is preferred to have a flow meter and a metering pump.
상기 컨트롤러(미도시)는 하수 재이용 장치의 모든 구성요소를 통합적으로 제어하며, 실시간 모니터링 및 피드백 제어, 원격제어가 가능하게 구성된다. The controller (not shown) integrally controls all components of the sewage reuse device, and is configured to enable real-time monitoring, feedback control, and remote control.
도 1에서 미설명부호 94는 각각 하수 집수조(10)에서 전기응집유닛(40)으로 하수를 압송하는 제1펌프이며, 미설명부호 95는 전기응집유닛(40)에서 1차 여과기(50)로 처리수를 압송하는 제2펌프이다. 그리고, 미설명부호 V1 ~ V15은 각 배관을 통한 하수 또는 처리수의 흐름을 제어하는 밸브들로, 상기 밸브들은 전동밸브 또는 공압밸브 등 공지의 밸브를 이용할 수 있는데, 상기 밸브로서 공압밸브를 이용하는 경우에는 상기 공압밸브는 상기 공기공급기(97)와 연결되어 공압을 인가받도록 구성되는 것이 바람직하다. In FIG. 1, reference numeral 94 denotes a first pump for pumping sewage from the sewage collecting tank 10 to the electrocoagulation unit 40, and reference numeral 95 is an electrocoagulation unit 40 to the primary filter 50. It is a 2nd pump which feeds process water. In addition, reference numerals V1 to V15 are valves for controlling the flow of sewage or treated water through respective pipes, and the valves may use a well-known valve such as an electric valve or a pneumatic valve. In this case, the pneumatic valve is preferably configured to be connected to the air supply 97 to receive the pneumatic pressure.
상기와 같이 구성된 하수 재이용 장치는 다음과 같이 작동한다. The sewage reuse device configured as above operates as follows.
도 2는 하수의 정수 처리가 이루어지는 과정을 나타낸 도면으로, 하수 집수조(10)에 하수가 일정 수위 저장되면, 제1펌프(94)가 가동되어 하수 집수조(10)의 산도(pH)가 조정된 하수가 공급배관(91)을 통해 유동한다. 이 때, 하수는 스크린(20)을 통과하면서 1차 협잡물이 걸러진 다음, 자기장발생기(30)에 의해 하수 분자가 미립자화된다. 2 is a view showing a process of water treatment of sewage, when the sewage is stored in the sewage collection tank 10 at a certain level, the first pump 94 is operated to adjust the pH (pH) of the sewage collection tank 10 Sewage flows through the supply pipe (91). At this time, the sewage is filtered through the screen 20 while the primary contaminants are filtered out, and the sewage molecules are granulated by the magnetic field generator 30.
상기 자기장발생기(30)를 통과한 하수는 전기응집 반응조(41) 하부의 유입구를 통해 전기응집 반응조(41) 내로 유입된다. 이 때, 전기응집 반응조(41) 내의 전원용 블레이드(44)에 전원이 인가되어 하수가 전기분해되고, 전극에서 용출된 금속이온들이 안정적으로 존재하는 입자들을 불안정화시킴과 동시에 플록화하여 오염물질을 제거하고 전기적 산화와 환원 반응으로 유해물질을 플록화하여 부상시킨다.The sewage that has passed through the magnetic field generator 30 is introduced into the electrocoagulation reactor 41 through an inlet port under the electrocoagulation reactor 41. At this time, the power is applied to the blade 44 for power in the electrocoagulation reactor 41, the sewage is electrolyzed, and the metal ions eluted from the electrode destabilize the particles stably present and at the same time floc to remove contaminants. And flocculate harmful substances by electrical oxidation and reduction.
이와 같이 전기응집 반응조(41) 내에서 전기응집 작용이 진행되는 동안 공기공급기(97)로부터 마이크로버블 산기관(42)에 압축공기가 공급되어 마이크로버블 산기관(42)에서 초미세 기포들이 방출된다. 상기 마이크로버블 산기관(42)에서 방출된 초미세 기포들은 전기응집 반응조(41) 내의 하수의 오염물 제거와 침전성 응집물(flocculate)의 부상을 원활하게 하여 블레이드(45)에 스케일이 흡착되는 것을 방지한다.In this way, the compressed air is supplied from the air supplier 97 to the microbubble diffuser 42 while the electrocoagulation action is performed in the electrocoagulation reactor 41, and ultra-bubbles are released from the microbubble diffuser 42. . The microbubbles released from the microbubble diffuser 42 facilitate the removal of contaminants of sewage and flotation of sedimentary flocculate in the electrocoagulation reactor 41 to prevent the scale from adsorbing to the blade 45. do.
상기 전기응집 반응조(41)에서 정수 처리된 처리수는 제2펌프(95)에 의해 1차 여과기(50) 및 2차 여과기(60)로 차례로 유입되어 잔여 응결물과 미처된 오염물들이 걸러진다. The treated water purified by the electrocoagulation reactor 41 is sequentially introduced into the primary filter 50 and the secondary filter 60 by the second pump 95 to filter out residual condensate and contaminants that have not been contaminated.
상기 2차 여과기(60)를 통과한 처리수는 공급배관(91)을 통해 처리수 집수조(80)로 보내지는데, 이 과정에서 오존발생기(71)에 의해 일정량의 오존이 주입되어 살균 처리가 이루어짐과 더불어 염소주입기(72)를 통해 일정량의 염소가 주입된다. The treated water passing through the secondary filter 60 is sent to the treated water collecting tank 80 through the supply pipe 91, in which a certain amount of ozone is injected by the ozone generator 71 to perform sterilization. In addition, a certain amount of chlorine is injected through the chlorine injector 72.
상기와 같은 과정을 거쳐 정수 처리된 처리수는 처리수 집수조(80)에 저장된 후 중수도 또는 다른 용도의 재이용수로서 재사용된다. The treated water treated through the above process is stored in the treated water collecting tank 80 and then reused as reused water for heavy water or other uses.
한편, 상술한 정수 처리 과정을 일정 시간 동안 수행한 후 1차 여과기(50) 및/또는 2차 여과기(60)가 세척되는 공정이 수행된다. 도 3에 도시된 것과 같이, 이 세척 공정에서는 공급배관(91)을 통한 하수의 유동이 차단되고, 역세용 배관(92)의 관로가 개방된다. 그리고, 제3펌프(96)가 동작하여 처리수 집수조(80) 내의 처리수가 역세용 배관(92)을 통해 1차 여과기(50) 및/또는 2차 여과기(60)로 압송된다. 1차 여과기(50) 및/또는 2차 여과기(60)로 공급되는 처리수는 1차 여과기(50) 및/또는 2차 여과기(60)의 배출구 쪽에서 유입되어 1차 여과기(50) 및/또는 2차 여과기(60)를 거꾸로 유동하면서 세척을 수행한 다음, 1차 여과기(50) 및/또는 2차 여과기(60)의 유입구 쪽에 연결된 드레인 배관(93)을 통해 하수관거로 방류된다. On the other hand, after performing the above-described purification process for a predetermined time is a process of washing the primary filter 50 and / or secondary filter 60 is performed. As shown in FIG. 3, in this washing process, the flow of sewage through the supply pipe 91 is blocked, and the pipeline of the backwashing pipe 92 is opened. Then, the third pump 96 is operated to pump the treated water in the treated water collecting tank 80 to the primary filter 50 and / or the secondary filter 60 through the backwashing pipe 92. The treated water supplied to the primary filter 50 and / or the secondary filter 60 flows in from the outlet side of the primary filter 50 and / or the secondary filter 60 so that the primary filter 50 and / or The washing is performed while the secondary filter 60 is flowed upside down and then discharged to the sewer pipe through a drain pipe 93 connected to the inlet side of the primary filter 50 and / or the secondary filter 60.
상기와 같이 1차 여과기(50) 및/또는 2차 여과기(60)에 대한 세척 공정을 수행할 때, 공기공급기(97)를 통해 1차 여과기(50) 및/또는 2차 여과기(60)로 압축공기를 공급하여 세척이 더욱 원활하게 이루어지도록 할 수 있다. When performing the washing process for the primary filter 50 and / or secondary filter 60 as described above, through the air supply 97 to the primary filter 50 and / or secondary filter 60 Compressed air can be supplied to make the cleaning more smooth.
또한, 상기 전기응집유닛(40)의 전기응집 반응조(41) 또한 주기적으로 세척이 필요한데, 먼저 전기응집 반응조(41) 내의 하수를 외부로 방류하여 전기응집 반응조(41) 내부를 비운 다음, 반응조세척기(43)로부터 세척수를 공급하고 설정 수위까지 채운다. 이 상태에서 설정 시간이 경과하면, 세척수를 외부로 방류하거나 다시 반응조세척기(43)로 회수시키면 세척이 완료된다. In addition, the electroagglomeration reactor 41 of the electrocoagulation unit 40 is also periodically required to clean, first discharge the sewage in the electrocoagulation reactor 41 to the outside to empty the inside of the electrocoagulation reactor 41, the reaction vessel washer Supply wash water from (43) and fill up to the set level. When the set time has elapsed in this state, the washing is discharged to the outside or recovered again to the reaction vessel washer 43, the washing is completed.
상술한 것과 같이, 본 발명의 하수 재이용 장치는 자기장발생기를 통해 전기응집유닛(40)으로 유입되는 하수의 분자를 미립자화시킴으로써 전기응집 작용이 더욱 원활하게 이루어져 처리 효율을 향상시킬 수 있는 이점이 있다. As described above, the sewage recycling apparatus of the present invention has an advantage that the electrocoagulation action can be made more smoothly by making particles of sewage flowing into the electrocoagulation unit 40 through a magnetic field generator, thereby improving treatment efficiency. .
그리고, 상기 전기응집 반응조(41) 내의 블레이드(45)의 표면이 특수 표면처리되어 미세한 엠보싱들이 형성되어 표면적이 넓어지므로 이온 용출이 더욱 원활하게 이루어지고, 이에 따라 전기응집 작용이 더욱 활발해져 처리 효율을 더욱 향상시킬 수 있으며, 전력소비를 감소시킬 수 있다. In addition, since the surface of the blade 45 in the electrocoagulation reactor 41 has a special surface treatment, fine embossing is formed to increase the surface area, ion elution is more smoothly performed, and thus the electrocoagulation action becomes more active, thereby improving treatment efficiency. It can be further improved, and power consumption can be reduced.
또한, 기존의 오폐수 처리장치와는 달리 별도의 처리조나 여과조를 두지 않고 연속적으로 반응하고 여과할 수 있도록 구성되어 있다. 따라서, 기존의 오폐수 처리장치와 같은 넓은 설치 면적이 필요치 않으며, 여러 구성부들을 패키지화시켜 콤팩트한 하수 재이용 장치를 구현할 수 있다. In addition, unlike the conventional wastewater treatment device is configured to continuously react and filter without placing a separate treatment tank or filtration tank. Therefore, a large installation area such as a conventional wastewater treatment apparatus is not required, and various components may be packaged to implement a compact sewage reuse device.
한편, 전술한 하수 재이용 장치의 실시예에서는 전기응집유닛(40)의 전기응집 반응조(41)를 하나로 구성하였으나, 이와 다르게 전기응집 반응조(41)를 복수개를 병렬로 구성할 수도 있을 것이다. On the other hand, in the above-described embodiment of the sewage recycling apparatus, the electroaggregation reactor 41 of the electroaggregation unit 40 is configured as one, but alternatively, the electroaggregation reactor 41 may be configured in plural in parallel.
본 발명은 다중 이용시설이나 산업체, 하수처리장 등에서 방류되는 하수를 정화시키는 하수 재이용 장치 또는 하수 정화장치에 적용될 수 있다. The present invention can be applied to a sewage reuse device or a sewage treatment device for purifying sewage discharged from a multi-use facility, an industry, a sewage treatment plant and the like.

Claims (6)

  1. 외부에서 공급되는 하수의 분자를 미립자화시키는 자기장발생기와;A magnetic field generator for atomizing the sewage molecules supplied from the outside;
    상기 자기장발생기를 통과하여 공급된 하수를 전기응집(electro-coagulation)에 의해 정수 처리하는 전기응집유닛과;An electrocoagulation unit for purifying the sewage supplied through the magnetic field generator by electro-coagulation;
    상기 전기응집유닛을 통해 정수 처리된 처리수에서 잔여 오염물을 걸러내는 여과기와;A filter for filtering out residual contaminants from the purified water through the electrocoagulation unit;
    상기 여과기를 통과한 처리수가 저장되는 처리수 집수조와;A treated water collecting tank for storing the treated water passing through the filter;
    일단이 상기 처리수 집수조에 연결되고 타단이 상기 여과기의 배출구 쪽에 연결되어 처리수 집수조의 처리수를 여과기로 공급하는 역세용 배관과;A backwashing pipe, one end of which is connected to the treatment water collection tank and the other end of which is connected to the outlet side of the filter to supply the treated water of the treatment water collection tank to the filter;
    상기 역세용 배관을 통해 상기 여과기로 세척을 위한 처리수를 압송하는 펌프와; A pump for pumping the treated water for cleaning to the filter through the backwashing pipe;
    상기 여과기의 유입구 쪽에 연결되어 여과기를 세척한 후 배출되는 처리수를 외부로 유도하는 드레인 배관과;A drain pipe connected to the inlet side of the filter to guide the treated water discharged after washing the filter to the outside;
    상기 여과기에 세척을 위한 압축공기를 공급하는 압축공기 공급유닛을 포함하여 구성된 것을 특징으로 하는 일체형 하수 재이용 장치.Integrated sewage recycling apparatus comprising a compressed air supply unit for supplying compressed air for cleaning to the filter.
  2. 제1항에 있어서, 상기 전기응집유닛은, The method of claim 1, wherein the electrocoagulation unit,
    외부로부터 하수를 공급받아 전기응집에 의해 하수를 정수하는 전기응집 반응조와; An electrocoagulation reactor for receiving sewage from the outside and purifying the sewage by electrocoagulation;
    상기 전기응집 반응조의 내부에 설치되며, 외부의 전원과 전기적으로 연결되어 전원을 인가받는 복수개의 전원용 블레이드와; A plurality of power supply blades installed in the electrocoagulation reactor and electrically connected to an external power source to receive power;
    상기 전원용 블레이드 사이에 배치되는 복수개의 금속재 블레이드와; A plurality of metal blades disposed between the power blades;
    상기 전기응집 반응조 내부의 하부에 설치되어 미세한 기포를 생성하는 마이크로버블 산기관을 포함하여 구성된 것을 특징으로 하는 일체형 하수 재이용 장치.Integral sewage recycling apparatus, characterized in that it comprises a microbubble diffuser installed in the lower portion of the electrocoagulation reactor to generate fine bubbles.
  3. 제2항에 있어서, 상기 전기응집유닛은 상기 전기응집 반응조의 세척을 위해 전기응집 반응조 내부로 세척수를 공급하는 반응조세척기를 더 포함하여 구성된 것을 특징으로 하는 일체형 하수 재이용 장치.3. The integrated sewage recycling apparatus according to claim 2, wherein the electrocoagulation unit further comprises a reaction vessel washer for supplying washing water into the electrocoagulation reactor for washing the electrocoagulation reactor.
  4. 제2항에 있어서, 상기 블레이드는 표면적을 증대시키기 위하여 표면에 미세한 엠보싱이 형성된 것을 특징으로 하는 일체형 하수 재이용 장치. 3. The integrated sewage recycling apparatus of claim 2, wherein the blade has fine embossing formed on its surface to increase its surface area.
  5. 제2항에 있어서, 상기 마이크로버블 산기관은 공기가 방출되는 미세한 기공이 형성된 다공성 중공관으로 이루어진 것을 특징으로 하는 일체형 하수 재이용 장치.The integrated sewage recycling apparatus according to claim 2, wherein the microbubble diffuser is made of a porous hollow tube having fine pores through which air is discharged.
  6. 제1항에 있어서, 상기 자기장발생기는 상기 전기응집유닛의 유입구에 장착되는 중공관 형태의 몸체와, 상기 몸체의 내주면의 상부 및 하부 각각에 장착되는 복수개의 반원통형 마그네트로 구성된 것을 특징으로 하는 일체형 하수 재이용 장치.The magnetic field generator of claim 1, wherein the magnetic field generator comprises a hollow tube-shaped body mounted at the inlet of the electrocoagulation unit, and a plurality of semi-cylindrical magnets mounted at upper and lower portions of the inner circumferential surface of the body. Sewage Recycling Device.
PCT/KR2010/005501 2009-08-31 2010-08-19 Integrated sewage reuse device WO2011025183A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020090081212A KR100943987B1 (en) 2009-08-31 2009-08-31 Integrated wastewater reusing system
KR10-2009-0081212 2009-08-31

Publications (2)

Publication Number Publication Date
WO2011025183A2 true WO2011025183A2 (en) 2011-03-03
WO2011025183A3 WO2011025183A3 (en) 2011-07-07

Family

ID=42182711

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2010/005501 WO2011025183A2 (en) 2009-08-31 2010-08-19 Integrated sewage reuse device

Country Status (2)

Country Link
KR (1) KR100943987B1 (en)
WO (1) WO2011025183A2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10526227B2 (en) * 2017-05-10 2020-01-07 Creative Water Solutions, Llc Wastewater treatment and solids reclamation system
US11104592B2 (en) 2018-05-18 2021-08-31 Creative Water Solutions, Llc Water treatment system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000036794A (en) * 2000-03-29 2000-07-05 김기영 A water softener using multimagnetic ceramics
KR20060128246A (en) * 2005-06-09 2006-12-14 주식회사 지에스인스트루먼트 Chamber blade module in electrochemical wastewater disposal apparatus
KR20060128243A (en) * 2005-06-09 2006-12-14 주식회사 지에스인스트루먼트 Electrochemical wastewater disposal apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000036794A (en) * 2000-03-29 2000-07-05 김기영 A water softener using multimagnetic ceramics
KR20060128246A (en) * 2005-06-09 2006-12-14 주식회사 지에스인스트루먼트 Chamber blade module in electrochemical wastewater disposal apparatus
KR20060128243A (en) * 2005-06-09 2006-12-14 주식회사 지에스인스트루먼트 Electrochemical wastewater disposal apparatus

Also Published As

Publication number Publication date
KR100943987B1 (en) 2010-03-02
WO2011025183A3 (en) 2011-07-07

Similar Documents

Publication Publication Date Title
CN205933558U (en) Processing apparatus of waste water
KR101162808B1 (en) Eco bio reactive system for water quality purification
KR100421515B1 (en) device for treatment of sewage
CN209957593U (en) Integrated efficient sewage membrane treatment equipment
CN215049222U (en) Chemical fiber textile dyeing wastewater treatment device
CN212246592U (en) Well water purification treatment equipment
WO2011025183A2 (en) Integrated sewage reuse device
CN100443034C (en) Showering water cyclic utilization system
CN210367354U (en) Water body multi-layer composite purification device
CN110054326A (en) Pressurized fluid electric flocculation sewage treatment process and system
CN212864409U (en) Water denitrification adsorption dephosphorization deep purification system
CN212924728U (en) Printing and dyeing wastewater pretreatment device
CN210237343U (en) Biochemical effluent treatment system
CN113443758A (en) Full-quantitative pretreatment device, treatment system and treatment method for landfill leachate
CN208345951U (en) A kind of electric flocculation heavy metal wastewater treatment apparatus
KR20110113984A (en) A smell remove device for car wash recycle water
RU109131U1 (en) STATION FOR ELECTROCOAGULATIVE PREPARATION OF DRINKING WATER WITH A WATER PRESSURE SYSTEM
KR100899330B1 (en) A ozone oxidation equipment and system using it
JP3309736B2 (en) Sewage treatment method and sewage treatment device
CN111320311B (en) Integrated concentric horizontal pipe electrochemical precipitation adsorption sewage treatment system
KR101544604B1 (en) SYSTEM FOR RECYClYING DISCHARGE WATER OF SEWAGE TREATMENT PLANT
RU6561U1 (en) WATER FLOW CLEANING DEVICE
CN218454135U (en) Laboratory wastewater treatment system
KR101967186B1 (en) Micro water membrane filter and filthy water reduction facility
CN214611952U (en) Sewage treatment system that membrane method fenton allies oneself with usefulness

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10812197

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 10812197

Country of ref document: EP

Kind code of ref document: A2