KR200456162Y1 - Underwater airation and underwater agitating device by control of rotating·backlashing - Google Patents

Underwater airation and underwater agitating device by control of rotating·backlashing Download PDF

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KR200456162Y1
KR200456162Y1 KR2020090001608U KR20090001608U KR200456162Y1 KR 200456162 Y1 KR200456162 Y1 KR 200456162Y1 KR 2020090001608 U KR2020090001608 U KR 2020090001608U KR 20090001608 U KR20090001608 U KR 20090001608U KR 200456162 Y1 KR200456162 Y1 KR 200456162Y1
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underwater
air
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reverse rotation
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KR20100008357U (en
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강대권
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주식회사 장호
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/14Activated sludge processes using surface aeration
    • C02F3/16Activated sludge processes using surface aeration the aerator having a vertical axis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/20Activated sludge processes using diffusers
    • C02F3/205Moving, e.g. rotary, diffusers; Stationary diffusers with moving, e.g. rotary, distributors
    • C02F3/207Moving, e.g. rotary, diffusers; Stationary diffusers with moving, e.g. rotary, distributors with axial thrust propellers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/308Biological phosphorus removal
    • 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
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Mixers Of The Rotary Stirring Type (AREA)
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Abstract

본 고안은 정·역회전 제어에 따른 수중교반 및 수중 폭기장치에 관한 것으로서, 오·폐수의 유기물 및 영양염류(질소, 인)를 제거하는 공정에서 단일 반응조내에 산소를 공급하여 유기물 제거 및 질산화를 위한 호기영역의 폭기기능과, 영양염류를 제거하기 위한 혐기영역의 교반기능이 정·역회전 제어에 따라 의해 이루어지도록 하는 것을 특징으로 한다. The present invention relates to an underwater agitation and underwater aeration device according to the forward and reverse rotation control, and to remove organic matter and nitrification by supplying oxygen in a single reactor in the process of removing organic matter and nutrients (nitrogen, phosphorus) from waste water. It is characterized in that the aeration function of the aerobic zone for, and the agitation function of the anaerobic zone for removing nutrients is made by the forward and reverse rotation control.

따라서 호기공정시 수중교반기의 임펠러를 역회전시켜 나선형 유속상승 장치를 통해 난류를 형성하여 산기관에서 발생되는 공기방울과 강하게 접촉시킴으로써 수두손실을 최소화하여 소요동력을 저감하고, 기액전달속도를 배가시켜 산소흡수율을 크게 상승시키는 특징이 있다.Therefore, during the aerobic process, the impeller of the underwater stirrer is reversed to form turbulent flow through the spiral flow rate increasing device, which makes strong contact with air bubbles generated from the diffuser, thereby minimizing head loss, reducing the required power, and doubling the gas-liquid transfer speed. There is a characteristic that greatly increases the oxygen absorption rate.

난류(TURBULENT FLOW), 수두(유체(流體)가 지니는 에너지를 길이의 단위), 수중교반기 Turbulent flow, head (the energy of a fluid unit of length), underwater stirrer

Description

정ㆍ역회전 제어에 따른 수중교반 및 수중 폭기장치{Underwater airation and underwater agitating device by control of rotating·backlashing} Underwater airation and underwater agitating device by control of rotating · backlashing}

본 고안은 정ㆍ역회전 제어에 따른 수중교반 및 수중 폭기장치에 관한 것으로서, 더욱 상세히 설명하면 오ㆍ폐수에 포함된 유기물 및 영양염류(질소, 인)를 제거하는 공정에서 단일 반응조내에 산소를 공급하여 유기물 및 영양염류 및 질산화를 위한 호기영역의 폭기기능과, 유기물 및 영양염류를 제거하기 위하여 정ㆍ역회전 제어에 따른 교반기능이 혐기영역에 마련되어 호기공정시 수중 교반기의 임펠러를 역회전시키면 나선형 유속상승 장치를 통해 난류(TURBULENT FLOW)를 형성되어 산기관에서 발생되는 공기방울과 유기물 및 영양염류를 강하게 접촉시킴으로써 수두손실을 최소화하여 소요동력을 저감하고, 기액전달속도를 배가시켜 산소흡수율을 크게 상승시키는 정ㆍ역회전 제어에 따른 수중교반 및 수중 폭기장치에 관한 것이다.The present invention relates to an underwater agitation and underwater aeration device according to forward and reverse rotation control, and more specifically, to supply oxygen into a single reaction tank in a process of removing organic matter and nutrients (nitrogen, phosphorus) contained in wastewater and wastewater. The aeration function of the aerobic zone for organic matter and nutrients and nitrification and the agitation function according to the forward and reverse rotation control to remove organic matter and nutrients are provided in the anaerobic zone. Turbulent flow is formed through the flow rate increasing device, so that the air bubbles generated from the diffuser and the organic matter and nutrients are strongly contacted to minimize head loss, thereby reducing the required power, and doubling the gas-liquid transfer rate to greatly increase the oxygen absorption rate. The present invention relates to an underwater agitation and underwater aeration device in accordance with forward and reverse rotation control.

현대사회가 공업화, 산업화되어 감에 따라 가정이나 산업현장에서 배출되는 오폐수는 그 량이나 오염도가 점차 증가하고 있는 추세이며, 그에 따라 오 폐수를 처리하기 위한 방법이나 시설을 위한 종래기술 또한 상당히 많이 나와 있다.As the modern society is industrialized and industrialized, the amount of wastewater discharged from homes and industrial sites is gradually increasing, and accordingly, there are quite a lot of conventional technologies for methods and facilities for treating wastewater. have.

일반적으로 오, 폐수를 처리하기 위해서 많이 쓰이는 방법은 화학적으로 처리하는 방법과 생물학적으로 처리하는 방법이 있다.In general, the most commonly used methods for treating wastewater and wastewater include chemical treatment and biological treatment.

화학적으로 처리하는 방법은 그 처리속도는 빠르나 화학약품에 의한 추가오염의 문제가 있으므로 생물학적으로 처리하는 방법이 널리 쓰이며, 그 중 활성오니법에 의한 방법이 활발히 연구되고 있다.The chemical treatment method is fast, but there is a problem of additional contamination by chemicals, so biological treatment is widely used. Among them, the active sludge method has been actively studied.

활성오니법이란 오폐수를 활성오니(호기성 세균)와 함께 폭기조에서 폭기, 교반하여 BOD(생물학적 산소요구량)를 거의 만족시키도록 하며, 하수 속의 콜로이드상이나 용해한 물질이 침전하거나 활성오니에 접착되어 깨끗한 물로 되는데 한 차례의 정화작용을 한 후, 침전된 물질을 분리하거나 필요에 따라 폐기 또는 다시 본처리 과정으로 반송하여 오폐수를 처리하는 방법을 말한다.The activated sludge method aerated and agitated the waste water in the aeration tank together with the activated sludge (aerobic bacteria) to almost satisfy BOD (biological oxygen demand), and colloidal or dissolved substances in sewage precipitate or adhere to the activated sludge to become clean water. It refers to a method of treating wastewater by separating the precipitated material after one purification operation and then discarding or returning it to the main treatment process if necessary.

또한, 활성오니법에 사용되는 폭기장치는 통상적으로 브로워(BLOWER)를 이용하여 강제적으로 공기를 공급하는 강제 급기식 수중폭기장치와, 단일 임펠러의 회전력에 의해 오수와 공기를 흡입시키는 자흡식 단일 임펠러형 수중폭기장치로 나누어진다.In addition, the aeration device used in the activated sludge method is a forced air submerged aeration device that normally supplies air by using a blower, and a self-contained single impeller that sucks sewage and air by the rotational force of a single impeller. It is divided into type underwater aeration system.

상기 강제 급기식 수중폭기장치는 공기 공급관과 연결하여 사용하고, 교반 및 급기 겸용으로 탈질 탈인처리를 할 수 있으며, 고효율 설계로 뛰어난 산소 전달 능력과 송기량을 증감 또는 단속운전함으로써 산소 공급량의 조절이 용이하다.The forced air type underwater aeration device is used in connection with an air supply pipe, and can be denitrified and dephosphorized by agitation and air supply, and the oxygen supply can be controlled by increasing or decreasing the oxygen supply capacity and the air flow rate with a high efficiency design. It is easy.

또한, 자흡식 단일 임펠러형 수중폭기장치 강한 지흡력으로 송풍기관련 배관이 필요 없어 설치 및 유지관리가 용이하고, 구조가 간단하여 고장 발생률이 낮으며, 소음이 적으므로 어느 장소에도 설치가 가능하다.In addition, the self-suction single impeller-type underwater aeration device does not need a blower-related piping due to strong suction force, easy to install and maintain, simple structure, low failure rate, low noise, can be installed anywhere.

그러나 상기 강제 급기식 수중폭기장치는 산소 전달률은 우수하나 이에 따른 브로와 및 배관 설비 등의 추가적인 부대설비가 많이 소요되는 문제점이 있다.However, the forced air-type underwater aeration device is excellent in oxygen transfer rate, but there is a problem in that additional auxiliary equipment such as browers and plumbing facilities are required.

또한, 자흡식 단일 임펠러형 수중폭기장치 또는 이중 임펠러형 수중폭기장치는 강제 급기식 폭기장치에 비해 별도의 브로워 및 배관 설비 등을 포함한 부대설비가 요구되지는 않으나, 단위동력(KW)당 산소 전달율이 강제 급기식에 비해 현저히 떨어지기 때문에, 생물학적으로 많은 량의 산소를 필요로 하여 미생물을 이용한 오폐수를 처리하는 수중폭기장치로서는 부적합하다.In addition, the self-contained single impeller-type aeration system or double impeller-type aeration system does not require additional equipment including a separate brower and plumbing facilities, compared to a forced air aeration system, but the oxygen transmission rate per unit power (KW) Since it is considerably inferior to this forced air supply type, it is not suitable as an underwater aeration apparatus which requires biologically large amounts of oxygen and treats wastewater using microorganisms.

따라서 상기와 같은 문제점을 해소하기 위한 본 고안의 목적은 단일 반응조내에서 상부에는 호기영역의 폭기기능과 하부에는 혐기영역을 위한 교반기능이 일체로 구비된 상태에서 교반기능의 정·역회전 제어에 의해 상호 보완적으로 다기능이 이루어지도록 하여 호기공정시 혐기영역에서 수중교반기의 임펠러를 역회전시키면 내부가 나선형인 유속상승 장치를 통해 발생되는 난류가 상승하여 산기관에서 발생되는 공기방울과 접촉시키는 수중교반 및 수중 폭기장치를 제공한다. Therefore, an object of the present invention for solving the above problems is to control the forward and reverse rotation of the stirring function in a state in which the aeration function of the aerobic region at the top and the agitation function for the anaerobic region at the bottom are integrally provided in a single reactor. Multi-function is complementary by rotating the impeller of the underwater stirrer in the anaerobic zone during the aerobic process, and the turbulence generated through the spiral flow rate riser rises and the water comes into contact with air bubbles generated from the diffuser. It provides a stirring and underwater aeration device.

이상에서 설명한 바와 같이 본 고안 수중교반 및 수중 폭기장치는 단일 반응조내에서 호기공정시 수중교반기의 임펠러를 역회전시켜 나선형 유속상승 장치를 통해 유기물 및 영양염류가 포함된 난류를 형성시켜 산기관에서 발생되는 공기방울 과 강하게 충돌시킴으로써 수두손실을 최소화하여 소요동력을 저감하고, 기액전달속도를 배가시켜 산소흡수율을 크게 상승시키는 효과가 있다.As described above, the present invention underwater agitator and underwater aeration device reversely rotate the impeller of the underwater agitator during aerobic process in a single reactor to form a turbulent flow containing organic matter and nutrients through a spiral flow riser to generate in the diffuser. By colliding strongly with the air bubbles, it is possible to minimize head loss and to reduce the required power, and to increase the oxygen absorption rate by doubling the gas-liquid transfer rate.

또한, 본 고안은 별도의 배관이 필요 없어 설치 및 유지관리가 용이하고, 구조가 간단하여 고장 발생률이 낮으며, 소음이 적으므로 어느 장소에도 설치할 수 있는 효과가 있다.In addition, the present invention does not require a separate pipe is easy to install and maintain, the structure is simple, the failure rate is low, the noise is low, there is an effect that can be installed in any place.

이하, 첨부된 도면에 의해 본 고안을 상세히 설명하면 다음과 같다.Hereinafter, the present invention by the accompanying drawings in detail as follows.

도 1은 본 고안 수중교반 및 수중폭기장치를 도시해 보인 분리 사시도 이고, 도 2는 본 고안 수중교반 및 수중폭기장치를 도시해 보인 결합사시도이고, 도 4는 본 고안 수중교반 및 수중폭기장치를 도시해 보인 결합단면도이다.1 is an exploded perspective view showing the present invention underwater stirring and underwater aeration apparatus, Figure 2 is a combined perspective view showing the present invention underwater agitating and underwater aeration apparatus, Figure 4 is a water agitator and underwater aeration apparatus It is the cross-sectional view shown.

본 고안 수중교반 및 수중폭기장치(1)는 오ㆍ폐수를 정화하기 위해 단일 반응조 내(10)에 설치하여 하부방향에서 상부방향으로 혐기영역(12), 완충영역, 호기영역(11)으로 구분하고, 혐기영역(12)에서는 교반기능과 호기영역(11)에는 폭기기능이 더 부가된다.Invented underwater stirring and underwater aeration device (1) is installed in a single reactor (10) to purify the waste water and wastewater, divided into anaerobic zone 12, buffer zone, aerobic zone (11) from the lower direction to the upper direction In the anaerobic region 12, the stirring function and the aerobic region 11 are further added to the aeration function.

따라서 상기 수중교반 및 수중폭기장치(1)중 유속상승장치(22)는 원통형상에 상ㆍ하부방향으로 대향지게 호퍼(35, 35')가 형성되어 장구형상을 이루고, 상기 원통형상의 내주면에는 길이방향으로 나선형(23)을 형성하여 교반되는 무기물 및 영양염류가 나선형(23)을 따라 빠르게 상승하는 과정에서 난류가 발생하여 상부로 공급하는 구조이다.Therefore, in the underwater stirring device and the aeration device 1, the flow rate increasing device 22 has a hopper 35, 35 'formed to face up and down in a cylindrical shape to form an janggu shape, and the length is formed on the inner circumferential surface of the cylindrical shape. In the process of forming a spiral 23 in the direction of the stirring mineral and nutrients along the spiral 23 is rapidly rising turbulence is generated and supplied to the top.

또한, 상기 유속상승장치(22)는 반응조(10)의 바닥에서 이격되도록 한 쌍의 받침대(36)를 마련하여 하부에 위치하는 호퍼(35')의 외주면으로 부착한다.In addition, the flow rate increasing device 22 is provided with a pair of pedestals 36 so as to be spaced apart from the bottom of the reaction tank 10 and attached to the outer circumferential surface of the hopper 35 'located below.

또한, 상기 유속상승장치(22)는 원통형상이기 때문에 내부로 삽입되는 수중교반기(33)가 내주면에 형성된 나선형(23)과 간격을 형성하고, 상기 수중교반기(33)의 하부 외주면에는 유속상승장치(22)의 하부 내주면에 고정하도록 고정부재(24)를 볼트 체결한다. In addition, since the flow rate increasing device 22 has a cylindrical shape, a water stirrer 33 inserted therein forms a gap with the spiral 23 formed on an inner circumferential surface thereof, and a flow rate increasing device is disposed on the lower outer circumferential surface of the water stirrer 33. The fixing member 24 is bolted to fix the lower inner peripheral surface of the 22.

상기 수중교반기(33)는 내부에 정ㆍ역회전하는 수중모터(30)가 수밀되게 설치된 상태에서 회전축(31)만 수직방향으로 외부로 노출되어 끝단에 임펠러(26)가 부착되도록 수중모터(30)를 밀폐하는 수밀케이싱(34)이 형성된다.The underwater stirrer 33 is an underwater motor 30 so that the impeller 26 is attached to the end by exposing the rotating shaft 31 to the outside in a vertical direction in a state where the underwater motor 30 that is forward and reversely rotated inside is tightly installed. ), A watertight casing 34 is formed.

상기 수밀케이싱(34)의 상부에는 수중교반기(33) 또는 수중교반 및 수중폭기장치(1)를 인양할 수 있도록 인양고리(28)와 수중모터(30)에 전원을 공급하는 리드선이 인출된다.The lead wire for supplying power to the lifting ring 28 and the underwater motor 30 is drawn out of the watertight casing 34 so as to lift the underwater stirrer 33 or the underwater stirrer and the underwater aeration device 1.

따라서 상기 수중교반기(33)는 유속상승장치(22) 내부로 관통되어 임펠러(26)는 유속상승장치(22)의 하부로 노출되어 받침대(36) 사이에 위치하고, 상부는 유속상승장치(22)의 상부로 돌출된 상태로 설치되는 게 바람직하다. Accordingly, the underwater stirrer 33 penetrates into the flow rate increasing device 22 so that the impeller 26 is exposed to the lower portion of the flow rate increasing device 22 and positioned between the pedestals 36, and the upper portion of the water speed increasing device 22 is located therein. It is preferable to be installed to protrude to the top of the.

또한, 상기 유속상승장치(22)의 상부에 형성된 호퍼(35) 둘레에는 수중교반기(33)와 수평하게 원형 또는 사각의 링형상을 갖는 공기배관(32)이 위치하고, 상기 공기배관(32)을 지지하기 위해서는 공기배관(32)의 저면과 받침대(36)의 상면 사이에 수직방향으로 각각의 포스트(25)가 부착되어 사방에서 고정한다. In addition, an air pipe 32 having a circular or square ring shape horizontally with the underwater stirrer 33 is positioned around the hopper 35 formed on the upper portion of the flow rate increasing device 22, and the air pipe 32 is disposed. To support, each post 25 is attached in a vertical direction between the bottom of the air pipe 32 and the top of the pedestal 36 to be fixed in all directions.

한편, 상기 공기배관(32)은 내부로 공기를 공급하여 유동할 수 있도록 통공되고, 상면 일측에는 도면에 미 도시 하였으나 공기호스와 연결되는 강제급기구(27)가 형성되어 공기를 외부에서 공급한다.On the other hand, the air pipe 32 is through the air to supply air to flow inside, although not shown in the figure on one side of the upper surface is provided with a forced air supply (27) connected to the air hose to supply air from the outside .

또한, 상기 공기배관(32)의 상면에는 일정간격으로 다수개의 산기관(21)이 부착되어 공기배관(32)으로 공급되어 유동하는 공기를 외부로 배출하여 공기방울(29)을 형성한다.In addition, a plurality of diffusers 21 are attached to the upper surface of the air pipe 32 at a predetermined interval to supply air to the air pipe 32 to discharge the flowing air to the outside to form air bubbles 29.

따라서, 본 고안 수중교반 및 수중 폭기장치(1)는 유기물 제거 및 질산화 공정의 호기영역(11)에서 임펠러(26)가 역회전하면서 내부가 나선형(23)인 유속상승장치(22)를 통해 난류가 형성되어 산기관(21)에서 발생되는 공기방울(29)과 무기물 및 영양염류가 강하게 충돌되고, 탈질화 및 탈인공정의 혐기영역(12)에서는 임펠러(26)를 정회전시켜 교반함으로서 반응을 촉진한다.Therefore, the present invention underwater stirring and underwater aeration device (1) is turbulent through the flow rate riser 22 of the spiral 23 inside the spiral while the impeller 26 reverse rotation in the aerobic region 11 of the organic matter removal and nitrification process Is formed to strongly collide with the air bubbles 29 generated in the diffuser 21 and the minerals and nutrients, and in the anaerobic region 12 of the denitrification and dephosphorization process, the impeller 26 is rotated forward and stirred to react. Promote.

도 3은 본 고안 유속상승장치를 도시해 보인 정면도면으로 원통형상으로 내주면에 나선형(23)이 형성되어 나선형(23)을 따라 상승속도를 가속하는 것은 물론 나선형(23)을 따라 상승하는 과정에 소용돌이 모양처럼 회전되어 난류가 발생하는 구조이다.Figure 3 is a front view showing the device designed to increase the flow rate of the spiral is formed on the inner circumferential surface in a cylindrical shape to accelerate the ascending speed along the spiral (23) as well as in the process of rising along the spiral (23) It is a structure that generates turbulence by rotating like a swirl.

도 5는 본 고안 수중교반 및 수중폭기장치의 실시 예를 도시해 보인 사용상태도이다. Figure 5 is a state diagram showing the embodiment of the present invention underwater stirring and underwater aeration apparatus.

본 고안은 정·역회전 제어에 따른 수중교반 및 수중 폭기장치(1)를 반응조(10)에 설치하여 오·폐수의 유기물 및 영양염류(질소, 인) 제거 공정에서 단일 반응조(10)내에 산소를 공급하여 유기물 제거 및 질산화를 위한 호기영역(11)에서 폭기기능이 부가되어 영양염류를 제거하기 위해 혐기영역(12)에서 교반기능을 갖는수중교반기(33)의 수중모터(30)를 호기공정시 수중교반기(33)의 임펠러(26) 를 역회전시키면 내부가 나선형인 유속상승 장치(22)를 통해 난류(TURBULENT FLOW)을 형성시켜 산기관(21)에서 발생되는 공기방울(29)과 강하게 충돌시킴으로써 수두손실을 최소화하여 소요동력을 저감하고, 기액전달속도를 배가시켜 산소흡수율을 크게 상승시키는 특징이 있다.The present invention is to install the underwater stirring and underwater aeration device (1) in the reaction tank (10) according to the forward and reverse rotation control to remove the organic matter and nutrients (nitrogen, phosphorus) of the waste water, oxygen in a single reaction tank (10) The aeration process is added to the aerobic motor (11) of the underwater stirrer (33) having a stirring function in the anaerobic zone (12) to remove nutrients by adding aeration in the aerobic zone (11) for removing organic matter and nitrification Reverse rotation of the impeller 26 of the underwater agitator 33 forms a turbulent flow through the spirally increasing flow rate device 22 to strongly form the air bubbles 29 generated in the diffuser 21. By minimizing head loss by reducing collision, the required power is reduced, and the oxygen absorption rate is greatly increased by doubling the gas-liquid transfer rate.

도 1은 본 고안 수중교반 및 수중폭기장치를 도시해 보인 분리 사시도.1 is an exploded perspective view showing the present invention underwater stirring and underwater aeration device.

도 2는 본 고안 수중교반 및 수중폭기장치를 도시해 보인 결합 사시도.Figure 2 is a perspective view showing a combination of the present invention underwater stirring and underwater aeration device.

도 3은 본 고안 유속상승장치를 도시해 보인 정면도.Figure 3 is a front view showing the present invention flow rate increase device.

도 4는 본 고안 수중교반 및 수중폭기장치를 도시해 보인 결합단면도.Figure 4 is a cross-sectional view showing the present invention underwater stirring and underwater aeration device.

도 5는 본 고안 수중교반 및 수중폭기장치의 실시 예를 도시해 보인 사용상태도.Figure 5 is a use state showing an embodiment of the present invention underwater stirring and underwater aeration device.

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

1: 수중교반 및 수중폭기장치 10: 반응조1: Underwater Stirring and Underwater Aerator 10: Reactor

11: 호기영역 12: 혐기영역11: aerobic zone 12: anaerobic zone

21: 산기관 22: 유속상승장치21: diffuser 22: velocity increasing device

23: 나선형 24: 고정부재23: spiral 24: fixing member

25: 포스트 26: 임펠러25: Post 26: Impeller

27: 강제급기구 28: 인양고리27: forced supply 28: lifting ring

29: 공기방울 30: 수중모터29: Air bubble 30: Submersible motor

31: 회전축 32: 공기배관31: rotating shaft 32: air piping

33: 수중교반기 34: 수밀케이싱33: Underwater Agitator 34: Watertight Casing

35, 35': 호퍼35, 35 ': Hopper

Claims (4)

삭제delete 단일 반응조(10)내에 삽입되어 바닥면과 이격되도록 받침대(36)가 부착되어, 반응조(10) 하부에 침전된 무기물 및 영양염류를 상부에 위치한 산기관(21)으로 상승시 난류를 형성하는 유속상승장치(22)와;Pedestal 36 is attached to be spaced apart from the bottom surface is inserted into a single reactor 10, the flow rate to form turbulence when the inorganic and nutrients precipitated in the lower portion of the reaction tank 10 to the diffuser 21 located in the upper portion A riser 22; 상기 유속상승장치(22)의 내부로 관통되게 삽입 설치된 수밀케이싱(34)은 상면에 인양고리(28)와, 내부에는 정ㆍ역회전이 가능한 수중모터(30)가 설치되고, 상기 수중모터(30)의 회전축(31) 끝단은 유속상승장치(22)의 하부로 노출되도록 임펠러(26)가 체결되어 역회전시 무기물 및 영양염류를 교반하여 유속상승장치(22)로 상승시키는 수중교반기(33)와;The watertight casing 34 inserted to be inserted into the flow rate increasing device 22 is provided with a lifting ring 28 on an upper surface thereof, and an underwater motor 30 capable of forward / reverse rotation therein, wherein the underwater motor ( The end of the rotation shaft 31 of the 30) is an underwater stirrer 33 to which the impeller 26 is fastened so as to be exposed to the lower portion of the flow rate increasing device 22, and then agitates minerals and nutrients during the reverse rotation to the flow rate increasing device 22. )Wow; 상기 유속상승장치(22)의 상부에는 상승하는 난류와 공기방울(29)이 충돌하도록 수밀케이싱(34)과 수평하게 위치하여 인입된 공기가 유동하도록 통공되는 공기배관(32)을 형성하고, 상기 공기배관(32) 내부로 공기를 공급하도록 일측 상면에 형성된 강제급기구(27)와, In the upper portion of the flow rate riser 22 is formed with an air pipe 32 which is positioned horizontally with the water-tight casing 34 so that the rising turbulence and the air bubbles 29 collide with each other, the air flows through the flow of the incoming air, A forced air supply 27 formed on an upper surface of the air pipe 32 to supply air into the air pipe 32; 상기 강제급기구(27)를 통해 공기배관(32)으로 공급되어 유동하는 공기를 외부로 배출하여 공기방울(29)을 형성하는 산기관(21)으로 구성된 수중교반 및 수중 폭기장치에 있어서, In the underwater stirring and underwater aeration device consisting of a diffuser (21) forming the air bubbles 29 by discharging the air flowing through the forced air supply 27 to the air pipe 32 to the outside, 상기 유속상승장치(22)는 원통형상으로 상ㆍ하부 끝단에는 대향지게 호퍼(35, 35')가 형성되고, 내주면에는 길이방향으로 나선형(23)을 형성하여 무기물 및 영양염류를 포함한 오폐수가 나선형(23)을 따라 상승할 때 난류가 발생하는 것을 특징으로 하는 정ㆍ역회전 제어에 따른 수중교반 및 수중 폭기장치.The flow rate increasing device 22 has a cylindrical shape, and hoppers 35 and 35 'are formed to face the upper and lower ends thereof, and a helical 23 is formed on the inner circumferential surface thereof in a longitudinal direction so that the wastewater including inorganic matter and nutrients is helical. Underwater stirring and underwater aeration apparatus according to the forward and reverse rotation control, characterized in that turbulence occurs when it rises along (23). 삭제delete 삭제delete
KR2020090001608U 2009-02-13 2009-02-13 Underwater airation and underwater agitating device by control of rotating·backlashing KR200456162Y1 (en)

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Citations (3)

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Publication number Priority date Publication date Assignee Title
JP2000024683A (en) 1998-07-07 2000-01-25 Ebara Corp Underwater agitating aerator
KR100583052B1 (en) * 2004-10-19 2006-05-26 한상배 Submersible Aerator with the Encreased Capacity of Aeration and Ability of Diffusion
KR100806994B1 (en) 2006-10-02 2008-02-25 한상배 Submersibe Aerator and Mixer with the Encreased Oxygen Transfer Rate and Stability

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000024683A (en) 1998-07-07 2000-01-25 Ebara Corp Underwater agitating aerator
KR100583052B1 (en) * 2004-10-19 2006-05-26 한상배 Submersible Aerator with the Encreased Capacity of Aeration and Ability of Diffusion
KR100806994B1 (en) 2006-10-02 2008-02-25 한상배 Submersibe Aerator and Mixer with the Encreased Oxygen Transfer Rate and Stability

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