KR101003162B1 - Stock raising onsite wastewater treatment apparatus - Google Patents

Stock raising onsite wastewater treatment apparatus Download PDF

Info

Publication number
KR101003162B1
KR101003162B1 KR1020080026503A KR20080026503A KR101003162B1 KR 101003162 B1 KR101003162 B1 KR 101003162B1 KR 1020080026503 A KR1020080026503 A KR 1020080026503A KR 20080026503 A KR20080026503 A KR 20080026503A KR 101003162 B1 KR101003162 B1 KR 101003162B1
Authority
KR
South Korea
Prior art keywords
treated water
tank
livestock wastewater
ozone
storage tank
Prior art date
Application number
KR1020080026503A
Other languages
Korean (ko)
Other versions
KR20090100962A (en
Inventor
송재윤
Original Assignee
(주)옥센텍
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 (주)옥센텍 filed Critical (주)옥센텍
Priority to KR1020080026503A priority Critical patent/KR101003162B1/en
Publication of KR20090100962A publication Critical patent/KR20090100962A/en
Application granted granted Critical
Publication of KR101003162B1 publication Critical patent/KR101003162B1/en

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/002—Construction details of the apparatus
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/78—Details relating to ozone treatment devices

Landscapes

  • 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)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

본 발명은 축산폐수에 초임계 상태로 오존을 혼합하여 축산폐수에 포함된 항생제 등 맹독성물질을 산화시킨 후에 미생물의 활성을 현저하게 증가시킬 수 있는 축산폐수 처리장치에 관한 것이다.

본 발명의 주요구성은 축산폐수에 포함된 협잡물을 걸러내어 축산폐수만이 배출시키는 협잡물처리조와, 협잡물처리조에서 협잡물이 처리된 축산폐수를 제공받아 저장하는 축산폐수저장조를 구비하는 통상의 축산폐수 처리장치에 있어서, 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받아 축산폐수에 포함된 혐기물을 제거하여 제1처리수로 방출하는 혐기조와; 제1처리수를 공급받아 오존과 혼합시켜 제1처리수에 포함되어 있는 항생제를 산화시켜 제거하여 제2처리수로 방출하는 오존반응조와; 제2처리수를 공급받아 공기(또는 산소)와 혼합시켜 제2처리수에 공기(또는 산소)를 공급하고, 미생물에 의해 유기물이 제거된 제3처리수를 방출하는 미생물조와; 제3처리수에 포함된 슬러지를 침전시키는 침전조를 포함하는 것을 특징으로 한다.

Figure R1020080026503

축산폐수, 오존, 항생제, 산소, 미생물, 침전조

The present invention relates to a livestock wastewater treatment apparatus capable of significantly increasing the activity of microorganisms after oxidizing a highly toxic substance such as antibiotics contained in the livestock wastewater by mixing ozone in a supercritical state.

The main constitution of the present invention is a conventional livestock wastewater having a livestock wastewater storage tank for filtering and collecting the impurities contained in the livestock wastewater to discharge only the livestock wastewater, and receiving and storing the livestock wastewater treated with the contaminants in the contaminant treatment tank. A treatment apparatus, comprising: an anaerobic tank supplied with livestock wastewater stored in the livestock wastewater storage tank to remove anaerobic matter contained in the livestock wastewater and discharged into the first treatment water; An ozone reaction tank receiving the first treated water, mixed with ozone to oxidize and remove the antibiotic contained in the first treated water, and to discharge it to the second treated water; A microbial tank that receives the second treated water and mixes it with air (or oxygen) to supply air (or oxygen) to the second treated water, and discharges the third treated water from which organic matter is removed by the microorganisms; It characterized in that it comprises a settling tank for depositing the sludge contained in the third treated water.

Figure R1020080026503

Livestock wastewater, ozone, antibiotics, oxygen, microorganisms, sedimentation tank

Description

축산폐수 처리장치{STOCK RAISING ONSITE WASTEWATER TREATMENT APPARATUS}Livestock Wastewater Treatment System {STOCK RAISING ONSITE WASTEWATER TREATMENT APPARATUS}

본 발명은 축산폐수에 초임계 상태로 오존을 혼합하여 축산폐수에 포함된 항생제 등 맹독성물질을 산화시킨 후에 미생물의 활성을 현저하게 증가시킬 수 있는 축산폐수 처리장치에 관한 것이다.  The present invention relates to a livestock wastewater treatment apparatus capable of significantly increasing the activity of microorganisms after oxidizing a highly toxic substance such as antibiotics contained in the livestock wastewater by mixing ozone in a supercritical state.

일반적으로 양계농장, 양돈농장, 젖소사육농장 등 각종 축산농장의 축사에서 배출되는 폐수는 환경오염을 상당히 가중시키기 때문에 정수처리를 하여 BOD, COD, 탁도를 최대한 낮춘 상태에서 배출하도록 법으로 규제하고 있으며, 이를위해 각종 축산폐수를 많이 방류하는 축산농장에서는 축산폐수 정화용 처리시설을 설치하여야만 한다.In general, wastewater discharged from livestock farms such as poultry farms, pig farms, and dairy farms increases the environmental pollution considerably, so it is regulated by law to discharge water at the lowest possible BOD, COD, and turbidity conditions by treating it with water. For this purpose, livestock farms that discharge a lot of livestock wastewater have to install treatment facilities for livestock wastewater purification.

한편, 축산폐수는 고농도이고, 일반 하수나 분뇨에 비하여 난분해성으로서 생물학적으로 축산폐수를 분해시키는데 소요시간이 길며, 질소농도가 유기물농도에 비하여 과다하게 높아서 영양 밸란스(Balance)가 맞지 않고, 축산농가에서 전염병예방을 위한 과다한 축사소독에 사용되는 축사소독약, 항생제 등이 포함되어 있어 질소 등을 처리하더도 항생제 등에 의해 미생물의 활동이 현저히 감소되어 처리시간이 장기간 소요되는 문제점이 있다.On the other hand, livestock wastewater is high in concentration, hardly decomposable compared to general sewage or manure, and it takes a long time to decompose livestock wastewater biologically, and nitrogen concentration is excessively higher than organic concentration, so nutrition balance is not met. The barn disinfectant used for excessive barn disinfection to prevent infectious diseases in farms, antibiotics, etc. are included, so even when treated with nitrogen, the activity of the microorganisms is significantly reduced by antibiotics, there is a problem that takes a long time to process.

본 발명의 목적은 축산폐수에 초임계 상태로 오존을 혼합하여 축산폐수에 포함된 항생제 등 맹독성물질을 산화시킨 후에 미생물의 활성을 현저하게 증가시킬 수 있는 축산폐수 처리장치를 제공하는 데 있다. SUMMARY OF THE INVENTION An object of the present invention is to provide a livestock wastewater treatment apparatus capable of significantly increasing the activity of microorganisms after oxidizing a highly toxic substance such as antibiotics contained in the livestock wastewater by mixing ozone in a supercritical state.

본 발명의 다른 목적은 슬러리가 제거된 축산폐수에 초임계상태로 오존을 혼합하여 COD, BOD, 색도 등을 기준치에 적합하게 조절하여 방류할 수 있는 축산폐수 처리장치를 제공하는 데 있다.Another object of the present invention is to provide a livestock wastewater treatment apparatus that can be discharged by adjusting the COD, BOD, chromaticity and the like to meet the standard value by mixing ozone in the supercritical state to the livestock wastewater from which the slurry is removed.

본 발명의 축산폐수 처리장치는 축산폐수에 포함된 협잡물을 걸러내어 축산폐수만이 배출시키는 협잡물처리조와; 협잡물처리조에서 협잡물이 처리된 축산폐수를 제공받아 저장하는 축산폐수저장조와; 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받아 축산폐수에 포함된 혐기물을 제거하여 제1처리수로 방출하는 혐기조와; 상기 제1처리수를 공급받아 오존과 혼합시켜 제1처리수에 포함되어 있는 항생제를 산화시켜 제거하여 제2처리수로 방출하는 오존반응조와; 상기 제2처리수를 공급받아 공기(또는 산소)와 혼합시켜 제2처리수에 공기(또는 산소)를 공급하고, 미생물에 의해 유기물이 제거된 제3처리수를 방출하는 미생물조와; 상기 제3처리수에 포함된 슬러지를 침전시키는 침전조; 및 제3처리수에 산소를 공급하여 산소포화농도를 증가시키는 후오존처리조;를 포함하며,
상기 혐기조는, 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받는 제1저장탱크와 흡입구와 배출구가 각각 상기 제1저장탱크의 내부에 위치하며 축산폐수를 강제로 순환시키는 순환펌프를 구비하고;
상기 오존반응조는, 상기 혐기물이 처리된 제1처리수를 내부로 공급받는 제2저장탱크와 상기 제1처리수를 흡입하는 제2펌프와, 제2펌프로 흡입된 상기 제1처리수와 외부로부터 오존을 각각 공급받아 상기 제1처리수와 오존을 혼합하는 혼합기와, 상기 혼합기에서 혼합된 혼합수를 상기 제2저장탱크의 내부로 배출하는 혼합관을 구비하고;
상기 미생물조는, 상기 오존반응조에서 배출되는 제2처리수를 내부로 공급받고 배출하는 제4저장탱크와 제4저장탱크에서 유기물을 제거하는 미생물과, 상기 제4저장탱크로 유입된 제2처리수를 흡입하는 제4펌프와, 상기 제4펌프로 흡입된 제2처리수와 외부로부터 공기(또는 산소)를 각각 공급받아 상기 제2처리수와 공기(또는 산소)를 혼합하는 제3혼합기와, 상기 제3혼합기에서 혼합된 혼합수를 상기 제4저장탱크의 내부로 배출하는 제3혼합관을 구비하고;
상기 침전조는, 상기 미생물조에서 배출된 제3처리수를 공급받아 제3처리수에 포함된 슬러지를 침전시키는 침전탱크와, 상기 미생물조에서 배출된 제3처리수를 상기 침전탱크로 공급하는 유입구와, 상기 침전탱크의 하부에 위치하며 유입된 제3처리수를 회전시키는 회전날개 및 침전된 슬러리를 제거하는 슬러리배출구를 구비하는 것을 특징으로 한다.An apparatus for treating livestock wastewater of the present invention comprises: a contaminant treatment tank configured to filter out contaminants contained in the livestock wastewater and discharge only the livestock wastewater; A livestock wastewater storage tank for receiving and storing the livestock wastewater in which the contaminants have been treated in the contaminant treatment tank; An anaerobic tank supplied with the livestock wastewater stored in the livestock wastewater storage tank to remove the anaerobic substances contained in the livestock wastewater and to discharge them to the first treated water; An ozone reaction tank receiving the first treated water and mixing it with ozone to oxidize and remove the antibiotic contained in the first treated water and to release it to the second treated water; A microbial tank which receives the second treated water and mixes it with air (or oxygen) to supply air (or oxygen) to the second treated water, and discharges the third treated water from which organic matter is removed by the microorganisms; A precipitation tank for precipitating sludge contained in the third treated water; And a ozone treatment tank for supplying oxygen to the third treated water to increase the oxygen saturation concentration.
The anaerobic tank includes a first storage tank for receiving livestock wastewater stored in the livestock wastewater storage tank and a circulation pump for inlet and outlet respectively located in the first storage tank to forcibly circulate the livestock wastewater;
The ozone reaction tank includes a second storage tank receiving the first treated water treated with the anaerobic substance therein, a second pump for sucking the first treated water, and the first treated water sucked into the second pump; A mixer for receiving ozone from the outside and mixing the first treated water and ozone, and a mixing tube for discharging the mixed water mixed in the mixer into the second storage tank;
The microbial tank includes microorganisms for removing organic matters from a fourth storage tank and a fourth storage tank which are supplied with and discharged the second treated water discharged from the ozone reaction tank, and the second treated water introduced into the fourth storage tank. A fourth pump for sucking the gas, a third mixer for receiving the second treated water sucked by the fourth pump and air (or oxygen) from the outside, respectively, and mixing the second treated water and air (or oxygen); A third mixing pipe for discharging the mixed water mixed in the third mixer into the fourth storage tank;
The settling tank includes a settling tank receiving the third treated water discharged from the microbial tank to precipitate sludge contained in the third treated water and an inlet for supplying the third treated water discharged from the microbial tank to the settling tank. And, located in the lower portion of the settling tank characterized in that it has a rotary blade for rotating the introduced third treated water and a slurry discharge port for removing the precipitated slurry.

삭제delete

삭제delete

바람직하게, 상기 혐기조는 유입된 축산폐수가 하부로만 이동되도록 제1혐기조와 제2혐기조로 분리시는 제1격벽과, 제1혐기조에 위치하는 제1순환펌프와, 제2혐기조에 위치하는 제2순환펌프로 이루어진 것을 특징으로 한다.Preferably, the anaerobic tank is a first bulkhead and a first circulation pump located in the first anaerobic tank and the second anaerobic tank separated into the first and second anaerobic tank so that only the livestock wastewater flows downward. It is characterized by consisting of a two-circulation pump.

바람직하게, 상기 오존반응조는 제2처리수를 제공받아 저장하는 제3저장탱크와 제2처리수를 흡입하는 제3펌프와, 제3펌프로 흡입된 제2처리수와 외부로부터 공기 또는 산소를 각각 공급받아 제2처리수와 공기 또는 산소를 혼합하는 제2혼합기와 제2혼합기에서 혼합된 제2혼합수를 제3저장탱크의 내부로 배출하는 제2혼합관로 이루어진 것을 특징으로 한다.Preferably, the ozone reactor is a third storage tank for receiving and storing a second treatment water, a third pump for sucking the second treatment water, the second treatment water sucked into the third pump and air or oxygen from the outside. And a second mixing tube receiving each of the second treated water and mixing air or oxygen, and a second mixing tube discharging the second mixed water mixed in the second mixer into the third storage tank.

바람직하게, 상기 혼합기는 경부가 점차적으로 축소되며 제1처리수 또는 제2처리수가 유입되는 상부축소관과, 외부로부터 오존 또는 공기(산소)가 유입되는 측면흡입관과, 상부축소관의 하부에 소정거리 이격되어 경부가 점차적으로 확대되며 상부로 유입되는 제1처리수 또는 제2처리수와 측면흡입관으로 유입되는 오존 또는 공기의 혼합물을 배출시키는 하부확대관으로 이루어진 것을 특징으로 한다.Preferably, the mixer is gradually reduced in diameter, the upper reduction tube into which the first treatment water or the second treatment water flows, the side suction tube into which ozone or air (oxygen) is introduced from the outside, and the lower portion of the upper reduction tube. The cervical part is gradually enlarged by being spaced apart from each other, and has a lower enlarged tube configured to discharge a mixture of ozone or air introduced into the first or second treated water and the side suction pipe into the upper portion.

바람직하게, 상기 침전조의 유입구는 침전탱크의 하부 일측에 형성된 것을 특징으로 한다.Preferably, the inlet of the settling tank is characterized in that formed on the lower side of the settling tank.

바람직하게, 침전조에서 배출되는 제4처리수를 내부로 공급받고 배출하는 제5저장탱크와 제5저장탱크로 유입된 제4처리수의 BOD, COD, 탁도 등을 체크하는 포화산소측정센서, 제5저장탱크의 제4처리수를 흡입하는 제5펌프와, 제5펌프로 흡입된 제4처리수와 외부로부터 오존를 각각 공급받아 제4처리수와 오존을 혼합하는 제4혼합기와 제4혼합기에서 혼합된 혼합수를 제5저장탱크의 내부로 배출하는 제4혼합관을 구비하는 후오존처리조를 더 포함하는 것을 특징으로 한다.Preferably, the saturated oxygen measuring sensor for checking the BOD, COD, turbidity, etc. of the fifth storage tank and the fourth treated water introduced into the fifth storage tank and supplied with the fourth treated water discharged from the sedimentation tank, 5 In the fifth pump for sucking the fourth treated water from the storage tank, the fourth treated water sucked by the fifth pump and the fourth mixer and the fourth mixer for mixing ozone from the fourth treated water by receiving ozone from the outside, respectively. It is characterized in that it further comprises a post ozone treatment tank having a fourth mixing pipe for discharging the mixed water mixed into the fifth storage tank.

본 발명에 따른 축산폐수 처리장치는 축산폐수에 초임계 상태로 오존을 혼합하여 축산폐수에 포함된 항생제 등 맹독성물질을 산화시켜 제거하여 미생물의 활성을 현저하게 증가시켜 처리시간을 단축시킬 수 있는 장점이 있다.Livestock wastewater treatment apparatus according to the present invention by mixing ozone in the livestock wastewater in a supercritical state by oxidizing and removing the poisonous substances such as antibiotics contained in the livestock wastewater to significantly increase the activity of the microorganisms to shorten the treatment time There is this.

또한, 미생물 처리 후 슬러리가 제거된 축산폐수에 초임계상태로 오존을 혼합하여 COD, BOD, 색도 등을 기준치에 적합하게 조절하여 방류할 수 있는 장점이 있다.In addition, by mixing ozone in the supercritical state in the livestock wastewater from which the slurry is removed after the microbial treatment, there is an advantage that can be discharged by adjusting the COD, BOD, chromaticity and the like appropriately to the reference value.

이하, 본 발명을 첨부된 도면을 이용하여 상세히 설명한다. Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.

도 1은 본 발명의 일실시예에 따른 축산폐수 처리장치의 블록도이고, 도 2는 본 발명에 따른 혼합기의 상세도이고, 도 3은 본 발명의 다른 실시예에 따른 축산폐수 처리장치의 블록도이며, 도 4는 본 발명에 따른 또다른 축산폐수 처리장치의 블록도이다.1 is a block diagram of a livestock wastewater treatment apparatus according to an embodiment of the present invention, Figure 2 is a detailed view of a mixer according to the present invention, Figure 3 is a block of a livestock wastewater treatment apparatus according to another embodiment of the present invention 4 is a block diagram of another livestock wastewater treatment apparatus according to the present invention.

도 1에 도시된 바와 같이, 본 발명의 축산폐수 처리장치는 축산폐수에 포함된 협잡물을 걸러내어 축산폐수만이 배출시키는 협잡물처리조(11)와; 협잡물처리조에서 협잡물이 처리된 축산폐수를 제공받아 저장하는 축산폐수저장조(12); 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받아 축산폐수에 포함된 혐기물을 제거하여 제1처리수로 방출하는 혐기조(20)와; 제1처리수를 공급받아 오존과 혼합시켜 제1처리수에 포함되어 있는 항생제를 산화시켜 제거하여 제2처리수로 방출하 는 오존반응조(30)와; 제2처리수를 공급받아 공기(또는 산소)와 혼합시켜 제2처리수에 공기(또는 산소)를 공급하고, 미생물에 의해 유기물이 제거된 제3처리수를 방출하는 미생물조(50)와; 제3처리수에 포함된 슬러지를 침전시키는 침전조(60) 및 상기 제3처리수에 포함된 슬러지를 침전시키는 침전조; 및 제3처리수에 산소를 공급하여 산소포화농도를 증가시키는 후오존처리조(70)를 구비한다.As shown in Figure 1, the livestock wastewater treatment apparatus of the present invention comprises a contaminant treatment tank (11) to filter out the impurities contained in the livestock wastewater to discharge only livestock wastewater; A livestock wastewater storage tank 12 for receiving and storing the livestock wastewater in which the contaminants have been treated in the contaminant treatment tank; An anaerobic tank (20) for receiving livestock wastewater stored in the livestock wastewater storage tank and removing the anaerobic substances contained in the livestock wastewater and discharging them to the first treated water; An ozone reaction tank 30 which receives the first treated water and mixes it with ozone to oxidize and remove the antibiotic contained in the first treated water and release the second treated water; A microbial tank 50 which receives the second treated water and mixes it with air (or oxygen) to supply air (or oxygen) to the second treated water, and discharges the third treated water from which the organic matter is removed by the microorganism; A settling tank 60 for precipitating sludge contained in the third treated water and a settling tank for precipitating sludge contained in the third treated water; And a post ozone treatment tank 70 for supplying oxygen to the third treated water to increase the oxygen saturation concentration.

협잡물처리조(11)는 축산폐수처리탱크 등으로부터 제공받은 축산폐수에 포함된 협잡물을 걸러내어 축산폐수만이 배출되도록 처리한다. The contaminant treatment tank 11 filters the contaminants contained in the livestock wastewater provided from the livestock wastewater treatment tank and the like so that only the livestock wastewater is discharged.

축산폐수저장조(12)는 협잡물처리조(11)에서 협잡물이 처리된 축산폐수를 제공받아 1차 저장한다. 이러한 축산폐수저장조(12)는 축산폐수의 처리용량에 따라 순차적으로 축산폐수를 제공할 수 있다.The livestock wastewater storage tank 12 receives the livestock wastewater from which the contaminants have been treated in the contaminant treatment tank 11 and stores the primary livestock wastewater. The livestock wastewater storage tank 12 may sequentially provide livestock wastewater according to the treatment capacity of the livestock wastewater.

혐기조(20)는 축산폐수저장조(12)에 저장된 축산폐수를 내부로 공급받고 배출하는 제1저장탱크(21)와 흡입구와 배출구가 각각 제1저장탱크(21)의 내부에 위치하며 축산폐수를 강제로 순환시키는 순환펌프(22)를 구비한다. 이러한 혐기조는 순환펌프(22)를 이용하여 축산폐수저장조(12)에 저장된 축산폐수를 내부로 공급받은 상태에서 순환펌프(22)로서 강제로 순환시켜 축산폐수에 포함된 인, 질소 등의 혐기물들을 방출시켜 제거하여 제1처리수로 방출한다. 이때, 순환펌프(22)의 흡입구와 배출구에 의해 혐기조로 유입된 축산폐수가 유동하게 되어 혐기조(20)의 바닥에 축산폐수의 침전물이 쌓이는 것을 방지된다. 또한, 상부를 개방시키면 방출되는 인, 질소 등의 혐기물 등이 쉽게 배출될 수 있다.The anaerobic tank 20 is a first storage tank 21 for supplying and discharging livestock wastewater stored in the livestock wastewater storage tank 12 and an inlet and an outlet are respectively located inside the first storage tank 21 to collect livestock wastewater. A circulation pump 22 forcibly circulated is provided. The anaerobic tank is forcibly circulated as a circulation pump 22 in a state in which livestock wastewater stored in the livestock wastewater storage tank 12 is supplied to the inside using the circulation pump 22, and anaerobes such as phosphorus and nitrogen contained in the livestock wastewater. It is discharged and removed to discharge into the first treated water. At this time, the livestock wastewater introduced into the anaerobic tank by the inlet and outlet of the circulation pump 22 flows to prevent accumulation of livestock wastewater on the bottom of the anaerobic tank 20. In addition, when the upper portion is opened, anaerobic substances such as phosphorus and nitrogen released may be easily discharged.

오존반응조(30)는 혐기물이 처리된 제1처리수를 내부로 공급받고 배출하는 오존반응탱크(31)와 제1처리수를 흡입하는 제2펌프(32)와, 제2펌프(32)로 흡입된 제1처리수와 외부로부터 오존(34)을 각각 공급받아 제1처리수와 오존을 혼합하는 혼합기(33)와 혼합기에서 혼합된 혼합수를 오존반응탱크(31)의 내부로 배출하는 혼합관(35)을 구비한다.The ozone reaction tank 30 has an ozone reaction tank 31 for supplying and discharging internally treated first treated water and a second pump 32 for sucking the first treated water, and a second pump 32. Receiving the first treatment water sucked into and the ozone 34 from the outside, respectively, the mixer 33 for mixing the first treatment water and ozone and discharge the mixed water mixed in the mixer into the ozone reaction tank 31 The mixing pipe 35 is provided.

도 2에 도시된 바와 같이, 혼합기(33)는 경부가 점차적으로 축소되며 제2펌프에서 흡입된 제1처리수가 유입되는 상부축소관(81)과, 외부의 오존발생장치에 연결되어 오존이 유입되는 측면흡입관(82)과, 상부축소관의 하부에 소정거리 이격되어 경부가 점차적으로 확대되며 제1처리수와 오존의 혼합물을 하부의 혼합관으로 배출시키는 하부확대관(83)으로 이루어진다. 이러한 혼합기(33)로 유입된 고압의 제1처리수는 상부축소관(81)을 통과하면서 유속이 매우 빨라지게 되어 측면흡입관(82)으로 오존을 강하게 흡입하여 혼합된다. 그 후, 하부확대관(83)을 통과한 제1처리수와 오존의 혼합물은 점점 확대되는 경부를 통과하면서 속도가 감소되어 제1처리수와 오존이 분자상태로 서로 혼합되어 혼합관(35) 및 오존반응탱크(31)에 체류하는 동안에 제1처리수에 포함되어 있는 항생제 등의 약제 및 무기물 등을 산화시켜 제거하여 제2처리수로 방출한다. As shown in FIG. 2, the mixer 33 is gradually reduced in diameter and connected to an upper reduction pipe 81 through which the first treated water sucked from the second pump flows, and an external ozone generating device so that ozone is introduced. The side suction pipe 82 is separated from the lower portion of the upper reduction tube by a predetermined distance, the neck portion is gradually enlarged and consists of a lower enlarged tube 83 for discharging the mixture of the first treatment water and ozone to the lower mixing tube. The first treatment water of high pressure introduced into the mixer 33 passes through the upper reduction tube 81, and the flow rate becomes very fast, and the ozone is strongly sucked into the side suction tube 82 and mixed. Thereafter, the mixture of the first treated water and ozone passing through the lower enlargement tube 83 is reduced in speed while passing through an enlarged neck portion, and the first treated water and ozone are mixed with each other in a molecular state so that the mixing tube 35 is mixed. And while staying in the ozone reaction tank 31, the medicament and inorganic substances such as antibiotics contained in the first treated water is oxidized and removed to release to the second treated water.

미생물조(50)는 오존반응조(30)에서 배출되는 제2처리수를 내부로 공급받고 배출하는 제4저장탱크(51)와 제4저장탱크(51)에서 유기물을 제거하는 미생물(미도시)과, 제4저장탱크(51)로 유입된 제2처리수를 흡입하는 제4펌프(52)와, 제4펌프(52)로 흡입된 제2처리수와 외부로부터 공기(또는 산소)(54)를 각각 공급받아 제2처리수와 공기(또는 산소)를 혼합하는 제3혼합기(53)와 제3혼합기(53)에서 혼합된 혼합수를 제4저장탱크(51)의 내부로 배출하는 제3혼합관(55)을 구비한다. 이와 같이 미생물조(50)는 유입된 제2처리수에 산소를 풍부한 제공할 수 있어 미생물들이 신속하게 유기물을 제거하여 제3처리수로 방출할 수 있다.The microorganism tank 50 is a microorganism (not shown) for removing organic matter from the fourth storage tank 51 and the fourth storage tank 51 to receive and discharge the second treated water discharged from the ozone reaction tank 30 therein. And the fourth pump 52 for sucking the second treated water introduced into the fourth storage tank 51, the second treated water sucked into the fourth pump 52 and air (or oxygen) 54 from the outside. ) Is supplied to each of the third mixer 53 and the third mixer 53 for mixing the second treated water and air (or oxygen) to discharge the mixed water mixed in the third mixer 53 into the fourth storage tank 51. Three mixing pipes 55 are provided. As described above, the microbial tank 50 may provide abundant oxygen to the introduced second treated water, so that the microorganisms may quickly remove the organic material and release it to the third treated water.

침전조(60)는 미생물조(50)에서 배출된 제3처리수를 공급받고 제3처리수에 포함된 슬러지를 침전시키는 침전탱크(61)와 침전탱크(61)의 하부에 위치하며 유입된 제3처리수를 회전시키는 회전날개(63) 및 침전된 슬러리를 제거하는 슬러리배출구(64)를 구비한다. 이때, 미생물조(50)에서 배출된 제3처리수가 유입되는 유입구(62)는 침전탱크의 하부 일측에 형성되어 슬러리는 자중에 의해 침전되어 상부에는 슬러리가 제거된 제4처리수가 배출되는 것이 바람직하다.The settling tank 60 is located at the bottom of the settling tank 61 and the settling tank 61 to receive the third treated water discharged from the microbial tank 50 and to settle the sludge included in the third treated water. 3, a rotary blade 63 for rotating the treated water and a slurry discharge port 64 for removing the precipitated slurry. In this case, the inlet 62 through which the third treated water discharged from the microorganism tank 50 is introduced is formed at one side of the lower side of the precipitation tank, and the slurry is precipitated by its own weight, and the fourth treated water from which the slurry is removed is discharged. Do.

후오존처리조(70)는 침전조(60)에서 배출되는 제4처리수를 내부로 공급받고 배출하는 제5저장탱크(71)와 제5저장탱크(71)로 유입된 제4처리수의 BOD, COD, 탁도 등을 체크하는 포화산소측정센서(72), 제5저장탱크(71)의 제4처리수를 흡입하는 제5펌프(73)와, 제5펌프(73)로 흡입된 제4처리수와 외부로부터 오존를 각각 공급받아 제4처리수와 오존을 혼합하는 제4혼합기(74)와 제4혼합기(74)에서 혼합된 혼합수를 제5저장탱크(71)의 내부로 배출하는 제4혼합관(76)을 구비한다. 이와 같이 후오존처리조(70)는 포화산소측정센서(72)에서 측정된 산소의 농도가 기준 이상이 될 때까지 제4처리수를 제4혼합기(74)로 순환시켜 미생물이 제거되고, 포화산소농도가 증가된 제5처리수로 변환하여 방출할 수 있다.After ozone treatment tank 70 is a BOD of the fourth treated water introduced into the fifth storage tank 71 and the fifth storage tank 71 to receive and discharge the fourth treated water discharged from the settling tank 60 therein. The fourth pump suctioned by the saturated oxygen measuring sensor 72 for checking the COD, the turbidity, the fourth treated water of the fifth storage tank 71, and the fourth suction sucked by the fifth pump 73. A fourth agent 74 which receives ozone from the treated water and the outside and discharges the mixed water mixed in the fourth mixer 74 and the fourth mixer 74 into the fifth storage tank 71. Four mixing pipes 76 are provided. As described above, the post ozone treatment tank 70 circulates the fourth treated water to the fourth mixer 74 until the concentration of oxygen measured by the saturated oxygen measuring sensor 72 becomes equal to or higher than the reference value, and microorganisms are removed. The oxygen concentration can be converted into the fifth treated water and discharged.

도 3에 도시된 바와 같이, 본 발명의 다른 실시예에 의하면, 혐기조(20)는 유입된 축산폐수가 하부로만 이동되도록 제1혐기조(20-1)와 제2혐기조(20-2)로 분리시키는 제1격벽(23)과, 제1혐기조(20-1)에 위치하는 제1순환펌프(22-1)와, 제2혐기조(20-2)에 위치하는 제2순환펌프(22-2)를 구비한다. 이와 같이 혐기조를 제1혐기조(20-1)와 제2혐기조(20-2) 등의 다수의 구획으로 분리시킨 상태에서 축산폐수저장조(12)에서 유입된 축산폐수의 혐기물은 제1협기조(20-1)에서 1차 제거시키고 제2혐기조(20-2)로 이동시켜 다시 2차 제거되도록 하여 혐기물의 제거효능을 향상시킬 수 있다. As shown in FIG. 3, according to another embodiment of the present invention, the anaerobic tank 20 is separated into a first anaerobic tank 20-1 and a second anaerobic tank 20-2 so that the livestock wastewater flows only downward. The first bulkhead 23, the first circulation pump 22-1 located in the first anaerobic tank 20-1, and the second circulation pump 22-2 located in the second anaerobic tank 20-2. ). As described above, the anaerobic wastewater introduced from the livestock wastewater storage tank 12 is separated into a plurality of compartments such as the first anaerobic tank 20-1 and the second anaerobic tank 20-2. In (20-1), the first removal and the second anaerobic tank (20-2) can be removed again to be removed again to improve the anaerobic removal efficiency.

또한, 오존반응조(30)는 제1처리수가 하부로만 이동되도록 오존반응탱크(31)와 잔류오존제거탱크(37)로 분리시키는 제2격벽(36)과, 오존반응탱크(31)의 제1처리수를 흡입하는 제2펌프(32)와, 제2펌프(32)로 흡입된 제1처리수와 외부로부터 오존(34)을 혼합하는 제1혼합기(33-1)와 제1혼합기에서 혼합된 혼합수를 오존반응탱크(31)의 내부로 배출하는 제1혼합관(35-1)을 잔류오존제거탱크(37)로 이동된 제2처리수를 흡입하는 제3펌프(38)와, 제3펌프(38)로 흡입된 제2처리수와 외부로부터 공기 또는 산소를 각각 공급받아 제2처리수와 공기 또는 산소를 혼합하는 제2혼합기(33-2)와 제2혼합기(33-2)에서 혼합된 제2혼합수를 잔류오존제거탱크(37)의 내부로 배출하는 제2혼합관(35-2)을 구비한다. 이때, 제2혼합기(33-2)는 혼합기와 동일한 구조를 갖으며, 제2혼합기(33-2)를 통과하면서 제2처리수와 공기 또는 산소가 분자상태로 서로 혼합되어 제2혼합관(35-2) 및 잔류오존제거탱크(37)에 체류하는 동안에 제2처리수에 포함되어 오존은 공기 또는 산소와 반응하면서 오존을 산소로 변환되어 신속하게 제거하여 후술하는 미생물조에서 미생물들이 오존에 의해 소멸되는 것을 방지할 수 있다.In addition, the ozone reaction tank 30 includes a second partition 36 separating the ozone reaction tank 31 and the residual ozone removal tank 37 so that the first treated water moves only downward, and the first of the ozone reaction tank 31. In the first pump 33-1 and the first mixer which mix the ozone 34 from the outside and the first treated water sucked into the second pump 32, and the second pump 32 which sucks the treated water. A third pump 38 for sucking the second treated water moved to the residual ozone removal tank 37 from the first mixed pipe 35-1 for discharging the mixed water to the inside of the ozone reaction tank 31; The second mixer 33-2 and the second mixer 33-2 which receive air or oxygen from the outside and the second treated water sucked into the third pump 38 and mix the second treated water and air or oxygen, respectively. And a second mixed pipe 35-2 for discharging the second mixed water mixed in the inside of the residual ozone removal tank 37. At this time, the second mixer 33-2 has the same structure as the mixer, and the second treated water and air or oxygen are mixed with each other in a molecular state while passing through the second mixer 33-2, so that the second mixer tube ( 35-2) and the ozone is contained in the second treated water while staying in the residual ozone removal tank 37, and ozone is converted into oxygen while reacting with air or oxygen to quickly remove the microorganisms. Extinction can be prevented.

한편, 도 4에 도시된 바와 같이, 본 발명의 축산폐수 처리장치는 모래여과기(80), 활성탄여과기(90), 역세수로(100)를 하나 또는 2개 이상 선택적으로 추가로 형성할 수 있다. 이러한 모래여과기(80) 또는 활성탄여과기(90) 또는 역세수로(100)를 통해 제5처리수에 포함되어 있을 수 있는 처리되지 않은 미생물 또는 유기물 등을 제거하여 방류할 수 있다.On the other hand, as shown in Figure 4, the livestock wastewater treatment apparatus of the present invention may selectively form one or two or more sand filter 80, activated carbon filter 90, backwash water path 100. . Through the sand filter 80, the activated carbon filter 90 or the backwash water passage 100 may be discharged by removing the untreated microorganisms or organic matter that may be included in the fifth treated water.

본 발명은 상술한 바람직한 실시예에만 한정되는 것이 아니라 본 발명의 요지를 벗어나지 않는 범위 내에서 여러 가지로 개량, 변경, 대체 또는 부가하여 실시할 수 있는 것임은 당해 기술 분야에 통상의 지식을 가진 자라면 용이하게 이해할 수 있을 것이다. 이러한 개량, 변경, 대체 또는 부가에 의한 실시가 이하의 첨부된 청구범위의 범주에 속하는 것이라면 그 기술사상 역시 본 발명에 속하는 것으로 간주한다.It is to be understood that the present invention is not limited to the above-described preferred embodiments, but can be practiced in various ways without departing from the spirit of the present invention in various ways. If you can easily understand. If the implementation by such improvement, change, substitution or addition falls within the scope of the appended claims below, the technical spirit is also regarded as belonging to the present invention.

도 1은 본 발명의 일실시예에 따른 축산폐수 처리장치의 블록도.1 is a block diagram of a livestock wastewater treatment apparatus according to an embodiment of the present invention.

도 2는 본 발명에 따른 혼합기의 상세도.2 is a detailed view of a mixer according to the present invention.

도 3은 본 발명의 다른 실시예에 따른 축산폐수 처리장치의 블록도.Figure 3 is a block diagram of a livestock wastewater treatment apparatus according to another embodiment of the present invention.

도 4는 본 발명에 따른 또다른 축산폐수 처리장치의 블록도.Figure 4 is a block diagram of another livestock wastewater treatment apparatus according to the present invention.

Claims (8)

삭제delete 축산폐수에 포함된 협잡물을 걸러내어 축산폐수만이 배출시키는 협잡물처리조와; 협잡물처리조에서 협잡물이 처리된 축산폐수를 제공받아 저장하는 축산폐수저장조와; 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받아 축산폐수에 포함된 혐기물을 제거하여 제1처리수로 방출하는 혐기조와; 상기 제1처리수를 공급받아 오존과 혼합시켜 제1처리수에 포함되어 있는 항생제를 산화시켜 제거하여 제2처리수로 방출하는 오존반응조와; 상기 제2처리수를 공급받아 공기(또는 산소)와 혼합시켜 제2처리수에 공기(또는 산소)를 공급하고, 미생물에 의해 유기물이 제거된 제3처리수를 방출하는 미생물조와; 상기 제3처리수에 포함된 슬러지를 침전시키는 침전조; 및 제3처리수에 산소를 공급하여 산소포화농도를 증가시키는 후오존처리조;를 포함하며, A contaminant treatment tank that filters out contaminants contained in the livestock wastewater and discharges only the livestock wastewater; A livestock wastewater storage tank for receiving and storing the livestock wastewater in which the contaminants have been treated in the contaminant treatment tank; An anaerobic tank supplied with the livestock wastewater stored in the livestock wastewater storage tank to remove the anaerobic substances contained in the livestock wastewater and to discharge them to the first treated water; An ozone reaction tank receiving the first treated water and mixing it with ozone to oxidize and remove the antibiotic contained in the first treated water and to release it to the second treated water; A microbial tank which receives the second treated water and mixes it with air (or oxygen) to supply air (or oxygen) to the second treated water, and discharges the third treated water from which organic matter is removed by the microorganisms; A precipitation tank for precipitating sludge contained in the third treated water; And a ozone treatment tank for supplying oxygen to the third treated water to increase the oxygen saturation concentration. 상기 혐기조는, 상기 축산폐수저장조에 저장된 축산폐수를 내부로 공급받는 제1저장탱크와 흡입구와 배출구가 각각 상기 제1저장탱크의 내부에 위치하며 축산폐수를 강제로 순환시키는 순환펌프를 구비하고;The anaerobic tank includes a first storage tank for receiving livestock wastewater stored in the livestock wastewater storage tank and a circulation pump for inlet and outlet respectively located in the first storage tank to forcibly circulate the livestock wastewater; 상기 오존반응조는, 상기 혐기물이 처리된 제1처리수를 내부로 공급받는 제2저장탱크와 상기 제1처리수를 흡입하는 제2펌프와, 제2펌프로 흡입된 상기 제1처리수와 외부로부터 오존을 각각 공급받아 상기 제1처리수와 오존을 혼합하는 혼합기와, 상기 혼합기에서 혼합된 혼합수를 상기 제2저장탱크의 내부로 배출하는 혼합관을 구비하고;The ozone reaction tank includes a second storage tank receiving the first treated water treated with the anaerobic substance therein, a second pump for sucking the first treated water, and the first treated water sucked into the second pump; A mixer for receiving ozone from the outside and mixing the first treated water and ozone, and a mixing tube for discharging the mixed water mixed in the mixer into the second storage tank; 상기 미생물조는, 상기 오존반응조에서 배출되는 제2처리수를 내부로 공급받고 배출하는 제4저장탱크와 제4저장탱크에서 유기물을 제거하는 미생물과, 상기 제4저장탱크로 유입된 제2처리수를 흡입하는 제4펌프와, 상기 제4펌프로 흡입된 제2처리수와 외부로부터 공기(또는 산소)를 각각 공급받아 상기 제2처리수와 공기(또는 산소)를 혼합하는 제3혼합기와, 상기 제3혼합기에서 혼합된 혼합수를 상기 제4저장탱크의 내부로 배출하는 제3혼합관을 구비하고;The microbial tank includes microorganisms for removing organic matters from a fourth storage tank and a fourth storage tank which are supplied with and discharged the second treated water discharged from the ozone reaction tank, and the second treated water introduced into the fourth storage tank. A fourth pump for sucking the gas, a third mixer for receiving the second treated water sucked by the fourth pump and air (or oxygen) from the outside, respectively, and mixing the second treated water and air (or oxygen); A third mixing pipe for discharging the mixed water mixed in the third mixer into the fourth storage tank; 상기 침전조는, 상기 미생물조에서 배출된 제3처리수를 공급받아 제3처리수에 포함된 슬러지를 침전시키는 침전탱크와, 상기 미생물조에서 배출된 제3처리수를 상기 침전탱크로 공급하는 유입구와, 상기 침전탱크의 하부에 위치하며 유입된 제3처리수를 회전시키는 회전날개 및 침전된 슬러리를 제거하는 슬러리배출구를 구비하는 것을 특징으로 하는 축산폐수 처리장치.The settling tank includes a settling tank receiving the third treated water discharged from the microbial tank to precipitate sludge contained in the third treated water and an inlet for supplying the third treated water discharged from the microbial tank to the settling tank. And, Livestock wastewater treatment apparatus characterized in that it comprises a slurry discharge port for removing the settled slurry and a rotary blade for rotating the third treated water introduced in the lower portion of the settling tank. 제2항에 있어서, The method of claim 2, 상기 혐기조는, 유입된 축산폐수가 하부로만 이동되도록 제1혐기조와 제2혐기조로 분리시는 제1격벽과, The anaerobic tank, the first partition wall when separating into the first anaerobic tank and the second anaerobic tank so that only the livestock wastewater flows down; 상기 제1혐기조에 위치하는 제1순환펌프와, A first circulation pump located in the first anaerobic tank, 상기 제2혐기조에 위치하는 제2순환펌프로 이루어진 것을 특징으로 하는 축산폐수 처리장치.Livestock wastewater treatment apparatus, characterized in that consisting of a second circulation pump located in the second anaerobic tank. 제2항에 있어서, The method of claim 2, 상기 오존반응조는, 상기 제2처리수를 제공받아 저장하는 제3저장탱크와, The ozone reaction tank, and the third storage tank for receiving and storing the second treated water, 상기 제2처리수를 흡입하는 제3펌프와, A third pump for sucking the second treated water; 상기 제3펌프로 흡입된 제2처리수와 외부로부터 공기 또는 산소를 각각 공급받아 제2처리수와 공기 또는 산소를 혼합하는 제2혼합기와, A second mixer which receives air or oxygen from the second treated water sucked into the third pump and the outside, respectively, and mixes the second treated water and air or oxygen; 상기 제2혼합기에서 혼합된 제2혼합수를 상기 제3저장탱크의 내부로 배출하는 제2혼합관로 이루어진 것을 특징으로 하는 축산폐수 처리장치.Livestock wastewater treatment apparatus comprising a second mixing pipe for discharging the second mixed water mixed in the second mixer into the third storage tank. 제2항에 있어서, The method of claim 2, 상기 침전조의 유입구는 상기 침전탱크의 하부 일측에 형성된 것을 특징으로 하는 축산폐수 처리장치.Livestock wastewater treatment apparatus, characterized in that the inlet of the settling tank is formed on the lower side of the settling tank. 제2항 내지 제4항 중 어느 하나의 항에 있어서, The method according to any one of claims 2 to 4, 상기 혼합기는 경부가 점차적으로 축소되며 제1처리수 또는 제2처리수가 유입되는 상부축소관과,The mixer is a narrowing portion is gradually reduced, and the upper reduction pipe to which the first treatment water or the second treatment water flows; 외부로부터 오존 또는 공기(산소)가 유입되는 측면흡입관과, A side suction pipe through which ozone or air (oxygen) flows from the outside, 상부축소관의 하부에 소정거리 이격되어 경부가 점차적으로 확대되며 상부로 유입되는 제1처리수 또는 제2처리수와 측면흡입관으로 유입되는 오존 또는 공기의 혼합물을 배출시키는 하부확대관으로 이루어진 것을 특징으로 하는 축산폐수 처리장치.The lower portion of the upper reduction tube is separated by a predetermined distance gradually expands the neck portion is characterized by consisting of a lower expansion tube for discharging a mixture of ozone or air introduced into the upper portion of the first treatment water or second treatment water and the side suction pipe. Livestock wastewater treatment device. 제2항에 있어서, The method of claim 2, 후오존처리조는, 상기 침전조에서 배출되는 제4처리수를 내부로 공급받고 배출하는 제5저장탱크와, After ozone treatment tank, and the fifth storage tank for supplying and discharging the fourth treatment water discharged from the settling tank therein, 상기 제5저장탱크로 유입된 제4처리수의 BOD, COD, 탁도 등을 체크하는 포화산소측정센서와, Saturated oxygen measuring sensor for checking the BOD, COD, turbidity, etc. of the fourth treated water introduced into the fifth storage tank, 제5저장탱크의 제4처리수를 흡입하는 제5펌프와, A fifth pump for sucking the fourth treated water of the fifth storage tank, 상기 제5펌프로 흡입된 제4처리수와 외부로부터 오존를 각각 공급받아 제4처리수와 오존을 혼합하는 제4혼합기와, A fourth mixer which receives ozone from the fourth treated water sucked into the fifth pump and the outside and mixes the fourth treated water and ozone, respectively; 상기 제4혼합기에서 혼합된 혼합수를 상기 제5저장탱크의 내부로 배출하는 제4혼합관을 구비하는 를 더 포함하는 것을 특징으로 하는 축산폐수 처리장치.Livestock wastewater treatment apparatus further comprising a fourth mixing pipe for discharging the mixed water mixed in the fourth mixer into the fifth storage tank. 제7항에 있어서, The method of claim 7, wherein 모래여과기, 활성탄여과기, 역세수로 및 이들의 순차적으로 연결된 장치의 어느 하나를 더 포함하는 것을 특징으로 하는 축산폐수 처리장치.Livestock wastewater treatment apparatus further comprises any one of a sand filter, an activated carbon filter, a backwash channel and a sequentially connected device thereof.
KR1020080026503A 2008-03-21 2008-03-21 Stock raising onsite wastewater treatment apparatus KR101003162B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020080026503A KR101003162B1 (en) 2008-03-21 2008-03-21 Stock raising onsite wastewater treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020080026503A KR101003162B1 (en) 2008-03-21 2008-03-21 Stock raising onsite wastewater treatment apparatus

Publications (2)

Publication Number Publication Date
KR20090100962A KR20090100962A (en) 2009-09-24
KR101003162B1 true KR101003162B1 (en) 2010-12-22

Family

ID=41359076

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020080026503A KR101003162B1 (en) 2008-03-21 2008-03-21 Stock raising onsite wastewater treatment apparatus

Country Status (1)

Country Link
KR (1) KR101003162B1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109231704A (en) * 2018-10-30 2019-01-18 黄心 A kind of method of the microbial bacteria flora of efficient degradation antibiotic and antibiotic of degrading
KR20210056842A (en) * 2019-11-11 2021-05-20 차태영 Purification system and method reinforced treament antibiotics
KR102311701B1 (en) * 2021-03-04 2021-10-13 이에스아이주식회사 Livestock manure treatment system using ozone dissolved water
KR20220064351A (en) * 2019-11-07 2022-05-18 한국수자원공사 a livestock excretion wastewater treatment method using both the oxidation and the coagulating process and the livestock excretion wastewater treatment system
KR102599985B1 (en) 2023-06-12 2023-11-08 (주)청수 Deaerating system of wastewater mixed with high concentration ammonia nitrogen

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102569770B1 (en) * 2018-11-09 2023-08-22 서부석 Animal Manure Disposal System using Hydroxide Radical
KR102528828B1 (en) * 2022-06-16 2023-05-04 (주)상원이엔씨 High concentration organic wastewater treatment method and apparatus using sbr process

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100325722B1 (en) 1999-12-08 2002-03-06 김윤 A treatment method of sewage and wastewater using ozone and oxygen
KR100414580B1 (en) * 2001-04-10 2004-01-07 주식회사 아이이아이 A purification system for a waste water of livestock
KR100462943B1 (en) 2002-10-07 2004-12-23 주식회사 아이이아이 The Waste disposal system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100325722B1 (en) 1999-12-08 2002-03-06 김윤 A treatment method of sewage and wastewater using ozone and oxygen
KR100414580B1 (en) * 2001-04-10 2004-01-07 주식회사 아이이아이 A purification system for a waste water of livestock
KR100462943B1 (en) 2002-10-07 2004-12-23 주식회사 아이이아이 The Waste disposal system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109231704A (en) * 2018-10-30 2019-01-18 黄心 A kind of method of the microbial bacteria flora of efficient degradation antibiotic and antibiotic of degrading
KR20220064351A (en) * 2019-11-07 2022-05-18 한국수자원공사 a livestock excretion wastewater treatment method using both the oxidation and the coagulating process and the livestock excretion wastewater treatment system
KR102616567B1 (en) * 2019-11-07 2023-12-22 한국수자원공사 a livestock excretion wastewater treatment method using both the oxidation and the coagulating process and the livestock excretion wastewater treatment system
KR20210056842A (en) * 2019-11-11 2021-05-20 차태영 Purification system and method reinforced treament antibiotics
KR102345686B1 (en) * 2019-11-11 2021-12-30 (주) 산해 Purification system and method reinforced treament antibiotics
KR102311701B1 (en) * 2021-03-04 2021-10-13 이에스아이주식회사 Livestock manure treatment system using ozone dissolved water
KR102599985B1 (en) 2023-06-12 2023-11-08 (주)청수 Deaerating system of wastewater mixed with high concentration ammonia nitrogen

Also Published As

Publication number Publication date
KR20090100962A (en) 2009-09-24

Similar Documents

Publication Publication Date Title
KR101003162B1 (en) Stock raising onsite wastewater treatment apparatus
US7018536B2 (en) Aerobic wastewater management system, apparatus, and method
US20080314828A1 (en) Apparatus and method for the treatment of waste
CN103214141A (en) Sewage advanced treatment and recycling method capable of substantially raising economy
CN106554131A (en) Integrated preposition denitrification sewage-treatment plant
CZ2005564A3 (en) Method for deep biological purification of waste water and apparatus to implement the same
US20050131266A1 (en) Carbonaceous waste treatment system and method
JPH11277091A (en) Apparatus and method for treating sewage/waste water by biological reaction
US3841997A (en) Dual aeration and filtration system with recycling
CN107555600A (en) A kind of sewage disposal system
KR101081302B1 (en) A method and apparatus for remove seston and nitrogen in wste water
KR102102437B1 (en) High speed oxidation device for the high concentration wastewater treatment
US20070221574A1 (en) System, method, and apparatus for aeration and processing waste in aerobic wastewater management
JP2006289153A (en) Method of cleaning sewage and apparatus thereof
US7022237B2 (en) Aerobic wastewater management system, apparatus, and method
CN209619128U (en) Municipal sewage plant vacuum in draft tube device
JP6369203B2 (en) Activated sludge treatment system
RU47002U1 (en) INTEGRATED WASTE WATER TREATMENT FROM POLLUTION
CN208545186U (en) A kind of countryside sewage treatment equipment
KR101632740B1 (en) Biological advanced treatment apparatus and method using an integrated aerobic nitrogen degassing
CN220174200U (en) Sewage draining device and system for dredging and bottom-cleaning of fishpond
JP2019171321A (en) Waste water treatment system and waste water treatment method
KR101180338B1 (en) a sewage disposal plant
CN205999245U (en) Plant's biogas slurry degraded equipment
RU2757589C1 (en) Method for purifying domestic waste water and station for implementation thereof

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20131210

Year of fee payment: 4

FPAY Annual fee payment

Payment date: 20150706

Year of fee payment: 5

R401 Registration of restoration
FPAY Annual fee payment

Payment date: 20150930

Year of fee payment: 6