KR102207832B1 - Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method - Google Patents

Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method Download PDF

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KR102207832B1
KR102207832B1 KR1020200029820A KR20200029820A KR102207832B1 KR 102207832 B1 KR102207832 B1 KR 102207832B1 KR 1020200029820 A KR1020200029820 A KR 1020200029820A KR 20200029820 A KR20200029820 A KR 20200029820A KR 102207832 B1 KR102207832 B1 KR 102207832B1
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treatment
decomposition
organic
organic waste
liquid
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서일봉
이일호
공성욱
이선일
김종학
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(주)상길테크
(주)정수
(주)인우코퍼레이션
김종학
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • 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
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/465Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electroflotation
    • 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
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
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    • 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
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/06Treatment of sludge; Devices therefor by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
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    • 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
    • C02F3/005Combined electrochemical biological processes
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    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00Fertilisers from human or animal excrements, e.g. manure
    • C05F3/06Apparatus for the manufacture
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F7/00Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

The present invention relates to an organic waste and waste liquid homogenization advanced pre-treatment apparatus and method. To this end, the apparatus of the present invention comprises: an organic waste treatment device (100) for removing hair or constricting substances unsuitable for a machine operation during raw excreta treatment; an active radical pressurization solubilizer device (200) for inducing separation of suspended substances through organic waste stabilization and solubilization; a dehydrated sludge treatment device (300) for separating sludge and an effluent to a non-agglomeration dewatering device; an active decomposition circulation device (400) for inducing oxidative decomposition through a contact free radical reaction with organic wastewater of an effluent; a decomposition flotation treatment device (500) for performing decomposition and flotation of dissolved complex oxides by pressure decomposition flotation; and an electrolysis oxidation coagulation flotation treatment device (600) for performing electrolysis oxidation coagulation sedimentation flotation after pressure decomposition and flotation. According to the present invention, before being separated into highly polluted organic waste and wastewater, a convergence and complex advanced pretreatment technology that can reduce the concentration of various pollutants, pathogens, viruses, and odors is provided. Accordingly, the quality and reliability of the advanced pre-treatment apparatus are greatly improved, and thus various demands (needs) of consumers who are users are satisfied. Thus, a good image can be impressed.

Description

유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법{Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method}Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method}

본 발명의 실시예는 유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법에 관한 것으로, 보다 상세하게는 오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술을 제공하는 것이며, 이로 인해 고도전처리 장치의 품질과 신뢰성을 대폭 향상시키므로 사용자인 소비자들의 다양한 욕구(니즈)를 충족시켜 좋은 이미지를 심어줄 수 있도록 한 것이다.An embodiment of the present invention relates to an apparatus and method for advanced pretreatment of organic waste and waste liquid homogenization, and more particularly, to reduce the concentration of various pollutants, pathogens, viruses, and odors before being separated into organic waste and wastewater having a high pollution concentration. Convergence/complex advanced pre-processing technology is provided, which greatly improves the quality and reliability of advanced pre-processing devices, so that a good image can be planted by satisfying the various needs (needs) of users.

주지하다시피 종래 각종 사업장에서 발생되는 슬러지(예: 일명 탈수케이크 등...)는 해양투기 방지법 시행규정규칙 개정으로 유기성 오니에 대한 해양배출규제가 슬러지를 2012년 1월부터 해양배출 전면 금지해 왔고 매립 또한 늘어남과 동시에 이차적인 환경오염이 누적되고 있는 문제가 심각 수준에 이르게 되어 현재 육상에서 슬러지 처리방안에 대한 강구가 불가피한 실정에 있다.As it is well known, conventional sludge (e.g., dehydrated cake, etc.) generated at various business sites has been completely banned from ocean discharge from January 2012 due to the amendment of the Enforcement Regulations of the Ocean Dumping Prevention Act. As landfills have also increased and secondary environmental pollution is accumulating, the problem has reached a serious level, so it is inevitable to devise a sludge treatment plan on land.

또한 유기성 폐기물 중 특히 가축분뇨처리 문제로 2019년 9월 현재 국내 한돈농가는 FTA로 인한 수입증대, 구제역 이후 돼지 사육두수 증가, 아프리카 돼지열병(ASF)으로 집단 살처분 및 이동조치 제안과 출하물량 저하로 생산비 이하의 돼지가격과 분뇨처리(슬러지) 반출금지로 가축분뇨 처분이 시급한 실정이며 돼지고기 가격과 소비위측이 계속되어 도산, 폐업이 잇따르고 있다. In addition, as of September 2019, domestic pig farms have increased imports due to FTA, increased pig breeding heads after foot-and-mouth disease, and proposed mass killing and movement measures due to African swine fever (ASF) and decreased shipments. Due to the price of pigs below the production cost and the prohibition of taking out manure treatment (sludge), the disposal of livestock manure is urgent, and the price and consumption of pork continue to rise, leading to bankruptcy and closure of business.

이렇게 슬러지 처리 방안에 시급한 실정에 있어 퇴비화, 부숙화, 소각화, 탄화, 건조화, 안정화처리, 고형화처리, 고형연료 등의 방법이 제시되고 있는데, 현재 가장시급한 것은 반출금지 및 이동제안으로 퇴비나 액비 그리고 위탁처리 또한 돼지열병으로 인해 농가에서는 자가처리 즉, 부숙화 및 안정화처리 하거나 정화방류로 자가 소비해야만하는 현실이 올지도 모른다는 예측되어지며, 현재 국내 자체처리 및 정화방류 축산농가는 5% 내외이며 대부분 퇴비와 액비는 위탁처리하고 있는 실정에 있다. In such an urgent situation for sludge treatment, methods such as composting, composting, incineration, carbonization, drying, stabilization treatment, solidification treatment, and solid fuel are being proposed.The most urgent thing currently is compost or liquid manure In addition, it is predicted that the consignment treatment may also come with a reality that farmers have to self-treat, that is, immature and stabilized treatment, or self-consumption through purified discharge due to swine fever. Currently, domestic self-treated and purified livestock farms are around 5%. Most of the compost and liquid manure are in consignment treatment.

앞으로 집단살처분, 이동제한 등으로 돼지가격급등, 물류비용인상, 농가 출입전 방역 전처리 부지확보, 처리통제에 따른 차단 및 통제 확보 등의 어려움이 있다.There are difficulties in securing pre-treatment sites for quarantine before entering and exiting farms, securing control and blocking according to treatment control, etc., due to genocide disposal and movement restrictions.

이러한 문제들로 인한 유기성 폐기물을 처리함에 있어 어디에 국한된 것은 아니고, 종래 각종 사업장에서 유기성폐기물을 육상에서 해결해야 한다는 것이다. 즉, 특히 악취를 동반한 슬러지 처리 문제가 현실적으로 시급하게 대두되고 있다.In the treatment of organic wastes due to these problems, it is not limited to any place, and conventionally, organic wastes must be resolved on land at various business sites. In other words, in particular, the problem of sludge treatment accompanied by odor is urgently emerging in reality.

현재 현황으로 검토된 육상 폐기물에 대한 대책으로 환경부에서는 복토재, 안정화처리, 건조, 탄화, 소각, 바이오매스, 자원화, 에너지화, 재활용을 연료화하여 매립부지의 고갈을 억제하고 환경적이면서 실증적인 슬러지 처리방안 대책을 각 지방 자치단체와 함께 최근 다각도로 개발되고 있는 것이 현 실정에 있지만, 어떤처리를 하든 현존하는 처리방식에서는 각각의 제2의 환경적 문제점을 가지고 있으며, 육상에서 발생되는 슬러지의 발생량과 처리효율로 볼 때 발생량을 효과적으로 줄일 수 있는 방안 및 기술의 적용성이 부족하여 환경부에서도 많은 개선을 요구하고 있지만 획기적인 방안보다는 규제강화와 더불어 단순히 건조감량을 통한 매립, 탄화, 소각처리를 할 수밖에 없는 상황이다.As a countermeasure for land waste reviewed as the current status, the Ministry of Environment uses cover material, stabilization treatment, drying, carbonization, incineration, biomass, resource conversion, energy conversion, and recycling as fuel to suppress the depletion of landfill sites and treat environmental and empirical sludge. Measures Measures are currently being developed in various angles with each local government, but the existing treatment methods each have a second environmental problem, and the amount of sludge generated on land and In terms of treatment efficiency, there is a lack of application of methods and technologies that can effectively reduce the amount of generation, and the Ministry of Environment is also demanding many improvements, but rather than a breakthrough method, it is inevitable that landfill, carbonization, and incineration are simply carried out through reduction in drying along with strengthening regulations. It is a situation.

또한 국내외 여러 가지 기술들을 검토되어 실행되고는 있으나 슬러지 감량화와 자원화 시스템처리 후 슬러지의 악취문제 및 부유물질 저감의 적용성이 떨어저 대규모 화력발전소 및 소각장에 협력처리하는 방식으로 검토 진행중에 있다.In addition, various technologies at home and abroad have been reviewed and implemented, but the odor problem of sludge and the applicability of reducing suspended solids after sludge reduction and recycling system treatment are inferior, so the review is under way by cooperative treatment with large-scale thermal power plants and incineration plants.

한편, 우리나라 실정에 유기성 폐기물 및 폐수처리하기에는 광범위한 부지와 폐수처리하기에는 일정한 폐수유입이 어려우며, 전처리의 다변화되는 오염부하를 컨트럴하기 어렵다.On the other hand, in Korea, it is difficult to control a wide range of sites for organic waste and wastewater treatment, and a certain amount of wastewater for wastewater treatment, and it is difficult to control the diversified pollution load of pretreatment.

종래 기술로, 국내 여타 기술은 대부분 생물반응처리 기반의 기술로 균질된 폐수를 습득하기에는 어려우며, 고도처리는 있지만 운영관리 또한 어렵다고 보아진다. 또한 국내 여타 조건의 처리방법을 다를 수 있는 전문인과 각가의 기술들이 적용공급한 현장에서도 생물반응 처리기술 이기에 현장적용에 큰 어려움이 따르며, 현장여건 및 생물조건에 따라 현장운영관리 또한 매우 어려운 실정이며, 특히 낙후된 가축분뇨처리 현장은 더 어려운 것이 현실이며, 효율적으로 현장에 실현가능하면서 발전가능한 방안제시의 기준이 없다는 것이 현실이다. As a conventional technology, most other technologies in Korea are based on bioreaction treatment, and it is difficult to obtain homogeneous wastewater, and it is considered that operation and management are difficult, although there is advanced treatment. In addition, because it is a bioreaction treatment technology in the field where specialists and individual technologies that may differ in the treatment method of other domestic conditions are applied and supplied, there is a great difficulty in the field application, and the field operation management is also very difficult depending on the site conditions and biological conditions. In particular, it is a reality that it is more difficult for an old livestock manure treatment site, and there is no standard for suggesting a plan that is feasible and developable at the site efficiently.

또한 전처리에 균질화가 안되어 부하가 갈수록 높아저 기존의 고도처리 또한 갈수록 적합한 폐수처리를 하기 위하여 고분자 응집제(폴리머)를 투여해서 처리하고는 있지만 관리하기도 어렵고 신개념에 처리장치도 또한 전처리의 부하로 증설해야하는 문제점이 발생 되었다.In addition, the pretreatment is not homogenized and the load is getting higher, so the existing advanced treatment is also treated by administering a polymer coagulant (polymer) to provide more and more suitable wastewater treatment, but it is difficult to manage, and the treatment device in a new concept must also be expanded under the load of pretreatment. A problem occurred.

그리고 기존의 전처리과정은 폐기물을 분리하기 위해 고분자 응집제를 첨가하여 폐기물을 탈수분리 하였지만 이러한 화학적 첨가제로 하여금 빠른 효과와 폐기물 및 폐수를 분리할 수 있었지만 이차적 분해가 어려운 폴리머 성분 때문에 생물반응처리의 처리효율은 떨어지고 농도 또한 높아지고 이름 모를 이상현상 즉, 삼층분리, 접착물질증가, 스컴, 점도증가, 침강성변화, 채류시간 등의 유지관리의 어려운 문제가 있었다.In addition, the existing pretreatment process dehydrated waste by adding a polymer coagulant to separate the waste, but these chemical additives were able to separate waste and wastewater with a quick effect, but the treatment efficiency of bioreaction treatment due to polymer components that are difficult to secondary decomposition. There was a difficult problem in maintenance such as three-layer separation, increase in adhesive material, scum, increase in viscosity, change in sedimentation, and retention time.

상기한 문제점을 해결하기 위해 종래에는 아래와 같은 선행기술문헌들이 개발되었으나, 여전히 상기한 종래 기술의 문제점을 일거에 해결하지 못하는 커다란 문제점이 발생 되었다.In order to solve the above problems, the following prior art documents have been developed in the prior art, but there is still a large problem that cannot solve the problems of the prior art at once.

대한민국 등록특허공보 제0478008호(2005. 03. 10)가 등록된바 있다.Republic of Korea Patent Publication No. 0478008 (2005. 03. 10) has been registered. 대한민국 등록특허공보 제0903062호(2009. 06. 09)가 등록된바 있다.The Republic of Korea Patent Publication No. 09303062 (2009. 06. 09) has been registered. 대한민국 등록특허공보 제1092017호(2011. 12. 02)가 등록된바 있다.Korean Registered Patent Publication No. 1092017 (2011. 12. 02) has been registered. 대한민국 등록특허공보 제1323277호(2013. 10. 23)가 등록된바 있다.Korean Registered Patent Publication No. 1323277 (2013. 10. 23) has been registered. 대한민국 등록특허공보 제2046833호(2019. 11. 14)가 등록된바 있다.Korean Patent Publication No. 2046833 (2019. 11. 14) has been registered.

본 발명은 상기와 같은 종래 기술의 제반 문제점을 해소하기 위하여 안출한 것으로, 유기성폐기물처리장치와 활성라디칼 가압 가용화장치 그리고 탈수슬러지 처리장치와 활성분해순환장치 그리고 분해부상처리장치와 전기분해 산화응집 부상처리장치가 구비됨을 제1목적으로 한 것이고, 상기한 기술적 구성에 의한 본 발명의 제2목적은 유기성폐기물의 협착물 및 이물질을 제거하고 유기성폐기물의 원물질부터 오염원을 저감시키기 위해 활성라디칼 가압교반 가용화하여 1차적으로 폐기물을 가용화 유기물이 분해된 농축수로 변화시키고 균질화한 상태에서 무응집 방식의 농축탈수기와 디스크 형식의 원심분리기를 통해 유기성폐기물(탈수슬러지)과 폐액(탈리액)을 폐수를 분리하여 유기성폐기물의 원물질부터 균질하게 오염농도 및 악취저감을 안정화시키는 고도전처리 통한 융·복합 처리방법을 제공하는 것이고, 제3목적은 이를 이용한 고도전처리로 국내에 여타 조건의 가축분뇨슬러지, 음식물슬러지,하·폐수 슬러지, 각종 사업장의 폐슬러지, 악취 발생되는 폐슬러지 및 폐수, 기타 발생되는 유기성 슬러지 및 폐수에 적용 가능하면서 국내 고도처리 공정에 병합시켜 지속적으로 발전가능한 고도전처리를 제공하는 것이고, 제4목적은 혐기조건의 유기성 폐기물을 안정적으로 가용화를 통해 오염농도와 슬러지를 감량화 저감시킨 후 균질화된 탈수슬러지와 탈리액(폐수)을 분리하고 폐수처리전에 활성라디칼 산화분해시켜 폐수처리 본 공정 즉, 생물반응조건에 균질하게 폐수를 조정해주는 고도전처리를 제공하는 것이고, 제5목적은 본 발명은 가용화에 있는 것으로 가용화라 함은 각각의 투입된 오존산화장치, 전기산화의 반응성의 성질을 이용하여 용존 가압믹싱하여 복합부유물질의 유기물을 우선적으로 슬러지의 바이러스, 병원균 등의 세포막 즉, 박테리아 세포속의 수분과 박테리아를 분해하고 결합수 사이의 내수분을 용존산화 믹싱을 통해 분산화 물리적 파쇄로 포화된 상태에서 산화반응의 환원되는 물수화물을 통해 가수분해되는 가용화 처리인 것으로, 슬러지처리시 각종오염원 들을 산화시켜 유기물을 분해하여 감량화 하고 악취와 동반된 복합물질을 저감시켜 균질화 하는데 있고, 특히 제6목적은 가용화기술을 통해 유기성 폐기물의 슬러지를 가압믹싱용 교반장치에 투입시켜 오존과 전기분해를 용존탱크에서 슬러지가 산화분해 되어지도록 하여 오염부유물질과 슬러지(유기물 SS)발생량을 감량화 시킨후 무응집 방식의 통상의 탈수기를 병합시킨 농축형 데칸타와 디스크형식 원심분리기를 통해 탈수슬러지와 탈리액으로 구분되어 균질된 부유물질과 악취가 저감된 슬러지와 탈리액으로 배출된 폐수에 활성라디칼 공정을 통해 균질된 폐수농도를 조절하고, PH조정한 뒤 가압분해 분리부상조로 하여금 잔존된 미세 유기물들을 분해 및 분리시킨 후 상부 분리된 슬러리는 집수조로 이송되어 리싸이클 하고 분리된 폐수는 오존과 함께 용존탱크에 가압 믹싱 용존 미세버블 순환장치를 통해 색도, 소독, 용존 가스제어 산화반응 탈질로 균질된 폐수를 습득하고 일정한 시간을 두워 잔존되어 있는 오존처리 후 균질된 페수를 기존의 생물반응조에 연계하는 유기성 폐기물 및 폐액 균질화 병합 고도전처리를 제공하게 되고, 제7목적은 고도전처리 슬러지 감량화로 배출되며, 특히 축산분뇨 자체를 처리하는 데는 악취저감 및 무응집방식으로 슬러지가 배출되어 부숙화, 퇴비화 등 자원 재활용할 가치의 발전가능한 균질된 목적물로 활용되기 위한 기존 선행 시설의 적용성 및 효율성을 극대화시키고 자원 재활용의 에너지원을 확보하며, 가장 큰 습득물은 냄새 안나는 슬러지로 배출된다는 점은 현재 모든 육상에서 발생된 폐기물을 육상에서 해결해야 한다는 것으로 볼 때 각종 민원과 상생가능한 진보적인 고도전처리처리 방법을 제공하는 것이고, 제8목적은 기존 기술들이 생물반응 구조의 바탕의 기준을 둔 기술로 사계절이 있는 우리나라에서는 참 유지관리 하기에는 한계가 있어 본 발명의 개발동기의 가장 큰 목적은 변화폭이 최소화 될 수 있게 기계와 전기적 설비장치로 하여금 생물반응 전에 악취, 부유물질, 독성물질, 난분해성, 부패성 유기물 및 기타 물질들을 최대한 감소시킬 수 있게 하였으며 그 효과는 향상시키면서 균질성은 확보된 고도전처리를 공정설비를 제공하여 생물반응 처리에 균질화된 전처리의 물질이 유입되도록 한 것이며, 제9목적은 국내유형으로 볼 때 갈수록 규제는 강화되어만 가는데 원인적인 전처리기준을 최적화시켜 후단부분에 부하를 줄이는 특화되어 있는 설비로 구성 되었으며, 현장 적용을 통한 융합기술을 최적화 한 고도전처리 표준화 기술을 제공하여 근본적인 인식구조를 변화시킬 수 있도록 한 것이고, 제10목적은 이로 인해 고도전처리 장치의 품질과 신뢰성을 대폭 향상시키므로 사용자인 소비자들의 다양한 욕구(니즈)를 충족시켜 좋은 이미지를 심어줄 수 있도록 한 유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법을 제공한다.The present invention was conceived to solve the problems of the prior art as described above, an organic waste treatment device, an activated radical pressure solubilization device, a dewatered sludge treatment device, an active decomposition circulation device, a decomposition flotation treatment device and an electrolysis oxidative aggregation floatation. The first purpose of the present invention is to provide a treatment device, and the second object of the present invention according to the above-described technical configuration is to remove contaminants and foreign substances from organic waste and to reduce pollutants from the raw material of organic waste. The wastewater is separated from organic waste (dehydrated sludge) and waste liquid (desorbed liquid) through a concentrated dehydrator of a non-aggregation method and a disk-type centrifuge in the state of solubilization and primary change of waste into concentrated water from which solubilized organic matter is decomposed. Therefore, it is to provide a fusion/combined treatment method through advanced pretreatment that homogeneously stabilizes pollution concentration and odor reduction from the raw material of organic waste, and the third purpose is to provide a high-level pretreatment using this to provide domestic animal manure sludge and food sludge under other conditions. It is applicable to sewage and wastewater sludge, waste sludge of various business sites, waste sludge and wastewater that generates odor, and organic sludge and wastewater that are generated, and provides advanced pretreatment that can be continuously developed by incorporating it into advanced domestic treatment processes. The purpose of 4 is to reduce and reduce pollution concentration and sludge through stable solubilization of organic waste under anaerobic conditions, separate homogenized dehydrated sludge and desorbed liquid (wastewater), and treat wastewater by oxidizing and decomposing activated radicals before wastewater treatment. It is to provide advanced pretreatment that homogeneously adjusts wastewater to conditions, and the fifth purpose of the present invention is to solubilize, and solubilization refers to dissolved and pressurized mixing using the properties of the reactivity of each input ozone oxidizing device and electric oxidation. The organic matter of the complex floating material is preferentially decomposed into cell membranes such as viruses and pathogens in the sludge, i.e., the moisture and bacteria in the bacteria cells, and the internal moisture between the bound water is dispersed through dissolved oxidation mixing and the oxidation reaction is performed in a saturated state by physical crushing. It is a solubilization treatment that is hydrolyzed through the reduced water hydrate, and oxidizes various pollutants during sludge treatment. It decomposes organic matter to reduce weight and reduces complex substances accompanied with odors to homogenize. In particular, the 6th purpose is to put the sludge of organic waste into the stirring device for pressurized mixing through solubilization technology, so that ozone and electrolysis are carried out in a dissolved tank. After the sludge is oxidatively decomposed to reduce the amount of contaminated suspended matter and sludge (organic SS) generated, it is divided into dehydrated sludge and dewatering liquid through a concentrated decanter incorporating a conventional dehydrator of a non-agglomeration method and a disk type centrifuge to be homogeneous. The wastewater discharged as sludge and desorption liquid with reduced suspended solids and odors is adjusted to a homogeneous wastewater concentration through an active radical process, adjusted PH, and then the pressure decomposition separation tank decomposes and separates the remaining fine organic matter. The separated slurry is transferred to a collection tank and recycled, and the separated wastewater is pressurized and mixed in the dissolved tank with ozone, through the dissolved microbubble circulator, chromaticity, disinfection, dissolved gas control, oxidation reaction, denitrification, and homogeneous wastewater are acquired and a certain amount of time is allowed. After the remaining ozone treatment, it provides advanced pretreatment combining organic waste and waste liquid homogenization by linking the homogeneous wastewater to the existing bioreactor, and the 7th purpose is discharged through advanced pretreatment sludge reduction, and especially for treating livestock manure itself. Maximizing the applicability and efficiency of existing pre-existing facilities and securing the energy source for resource recycling to be used as a homogeneous object capable of developing the value of resource recycling, such as odor reduction and non-aggregation method, as sludge is discharged, The biggest finding is that it is discharged as odorless sludge, which is to provide a progressive advanced pretreatment method that can coexist with various civil complaints, as it is considered that all waste generated on land must be resolved on land. This is a technology based on the bioreaction structure, and in Korea, where there are four seasons, there is a limit to true maintenance, so the main purpose of the development motivation of the present invention is to enable mechanical and electrical equipment to minimize the variation before bioreaction. Odor, suspended substances, toxic substances, hardly degradable, perishable organic substances and other substances It was possible to reduce the effect as much as possible, and to improve the effect and to provide a process facility for high-level pretreatment with secured homogeneity so that homogenized pretreatment materials flow into the bioreaction treatment. It is composed of specialized facilities that reduce the load at the rear end by optimizing the pretreatment standards that are causing it to be reinforced, and it provides advanced pretreatment standardization technology that optimizes convergence technology through field application, so that the fundamental recognition structure can be changed. The 10th objective is to provide an advanced pretreatment device and method for homogenizing organic waste and waste liquid so that a good image can be planted by satisfying the diverse needs (needs) of users as users, as it significantly improves the quality and reliability of advanced pretreatment devices. do.

이러한 목적 달성을 위하여 본 발명은 오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술인 유기성 폐기물 및 폐액 균질화 고도전처리 장치에 관한 것으로, 상기 유기성 폐기물 및 폐액 균질화 고도전처리 장치는, 원분뇨처리시 털이나 기계가동에 부적합한 협착물질을 제거하는 유기성폐기물 스크린처리장치와, 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 활성라디칼 가압 가용화장치와, 무응집 방식의 탈수장치로 슬러지와 탈리액을 분리하는 탈수슬러지 처리장치와, 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 활성분해순환장치와, 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 분해부상처리장치와, 가압분해 부상분리 처리 후 전기분해 산화응집부상처리하는 전기분해 산화응집 부상처리장치;가 순차적으로 연결 포함됨을 특징으로 하는 유기성 폐기물 및 폐액 균질화 고도전처리 장치를 제공한다.In order to achieve this object, the present invention relates to an advanced pretreatment apparatus for homogenizing organic waste and waste liquid, which is a fusion/complex advanced pretreatment technology capable of reducing the concentration of various pollutants, pathogens, viruses and odors before being separated into organic waste and wastewater with high pollution concentration. The organic waste and waste liquid homogenization advanced pretreatment device includes an organic waste screen treatment device that removes hairs or confining substances unsuitable for machine operation during raw manure treatment, and an active radical that induces separation of suspended substances through stabilization and solubilization of organic waste. A pressurized solubilization device, a dewatered sludge treatment device that separates sludge from a dewatering device with a non-aggregation type dehydration device, an active decomposition circulation device that induces oxidation and decomposition through a free radical reaction in contact with the organic wastewater of the desorbing liquid, and a pressurized decomposition flotation treatment. An organic waste, characterized in that a decomposition flotation treatment device for decomposing and flotation treatment of dissolved complex oxide substances, and an electrolysis oxidative flotation treatment device for electrolysis oxidative flotation treatment after pressure decomposition flotation treatment; A waste liquid homogenization advanced pretreatment device is provided.

또한 본 발명은 유기성 폐기물 처리대상물질을 협착물제거용 스크린을 이용하여 털이나 이물질만을 분리하여 집수조로 공급하는 단계(S10); 이후 축산분뇨의 유기물을 분해하여 가용화하는 활성라디칼 가압 가용화장치를 이용하여 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 단계(S20); 이어서 가용화처리된 분뇨 무약주(무응집: 응집제를 주입하지 않음) 탈수슬러지 처리장치를 이용하여 슬러지와 탈리액을 분리하는 단계(S30); 이후 오존발생장치가 포함된 활성분해순환장치를 이용하여 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 단계(S40); 이어서 분해부상처리장치를 이용하여 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 단계(S50); 이후 전기분해 산화응집 부상처리장치를 이용하여 유기성 폐기물 특성에 따라 복합 또는 개별장치로 용해성 콜로이드입자 전과 후처리로 오존산화 미세버블 및 전기분해 산화 응집부상 마이크로 버블처리로 난분해성 물질과 색도분해유도하는 단계(S60);가 포함됨을 특징으로 하는유기성 폐기물 및 폐액 균질화 고도전처리 방법을 제공한다.In addition, the present invention comprises the steps of separating only hairs or foreign substances by using a screen for removing organic waste materials to be treated and supplying them to a collection tank (S10); Thereafter, the step of inducing the separation of suspended substances through the stabilization and solubilization of organic wastes using an activated radical pressure solubilization device that decomposes and solubilizes organic substances in livestock manure (S20); Subsequently, separating the sludge and the desorption liquid using the solubilized manure-free liquor (no coagulation: no coagulant is injected) dewatered sludge treatment device (S30); Thereafter, the step of inducing oxidative decomposition through a contact free radical reaction with organic wastewater of the desorption liquid using an active decomposition circulation device including an ozone generator (S40); Subsequently, the step of decomposing and treating the complex oxide material dissolved by the pressure decomposition flotation treatment using a decomposition flotation treatment device (S50); Afterwards, using the electrolysis oxidation coagulation flotation treatment device, depending on the characteristics of organic wastes, the ozone oxidation microbubbles and electrolysis oxidation coagulation flotation microbubbles are treated as complex or individual devices before and after treatment. Step (S60); It provides an organic waste and waste liquid homogenization advanced pretreatment method characterized in that it is included.

상기에서 상세히 살펴본 바와 같이 본 발명은 유기성폐기물처리장치와 활성라디칼 가압 가용화장치 그리고 탈수슬러지 처리장치와 활성분해순환장치 그리고 분해부상처리장치와 전기분해 산화응집 부상처리장치가 구비되도록 한 것이다.As described in detail above, the present invention is to provide an organic waste treatment device, an activated radical pressure solubilization device, a dewatered sludge treatment device, an active decomposition circulation device, a decomposition flotation treatment device, and an electrolysis oxidation coagulation flotation treatment device.

상기한 기술적 구성에 의한 본 발명은 유기성폐기물의 협착물 및 이물질을 제거하고 유기성폐기물의 원물질부터 오염원을 저감시키기 위해 활성라디칼 가압교반 가용화하여 1차적으로 폐기물을 가용화 유기물이 분해된 농축수로 변화시키고 균질화한 상태에서 무응집 방식의 농축탈수기와 디스크 형식의 원심분리기를 통해 유기성폐기물(탈수슬러지)과 폐액(탈리액)을 폐수를 분리하여 유기성폐기물의 원물질부터 균질하게 오염농도 및 악취저감을 안정화시키는 고도전처리 통한 융·복합 처리방법을 제공하는 것이다.The present invention according to the above technical configuration is to remove contaminants and foreign substances of organic waste and to reduce the pollutant source from the raw material of organic waste, by solubilizing by active radical pressure stirring and solubilizing the waste firstly solubilizing the waste into concentrated water from which organic matter is decomposed. In a homogenized state, organic waste (dehydrated sludge) and waste liquid (desorbed liquid) are separated from the organic waste through a concentrated dehydrator in a non-aggregation method and a disk-type centrifuge to homogeneously stabilize the contamination concentration and odor reduction from the raw material of organic waste. It is to provide a fusion/complex treatment method through advanced pretreatment.

본 발명은 이를 이용한 고도전처리로 국내에 여타 조건의 가축분뇨슬러지, 음식물슬러지, 하·폐수 슬러지, 각종 사업장의 폐슬러지, 악취 발생되는 폐슬러지 및 폐수, 기타 발생되는 유기성 슬러지 및 폐수에 적용 가능하면서 국내 고도처리 공정에 병합시켜 지속적으로 발전가능한 고도전처리를 제공하는 것이다.The present invention can be applied to domestic animal manure sludge, food sludge, sewage/wastewater sludge, waste sludge of various business sites, waste sludge and wastewater generating odor, and other organic sludge and wastewater generated by advanced pretreatment using the same. It is to provide advanced pretreatment that can be continuously developed by incorporating it into domestic advanced treatment processes.

또한 본 발명은 혐기조건의 유기성 폐기물을 안정적으로 가용화를 통해 오염농도와 슬러지를 감량화 저감시킨 후 균질화된 탈수슬러지와 탈리액(폐수)을 분리하고 폐수처리전에 활성라디칼 산화분해시켜 폐수처리 본 공정 즉, 생물반응조건에 균질하게 폐수를 조정해주는 고도전처리를 제공하는 것이다.In addition, the present invention reduces the pollution concentration and sludge by stably solubilizing organic waste under anaerobic conditions, and then separates the homogenized dehydrated sludge and the desorption liquid (wastewater). It provides advanced pretreatment that homogeneously adjusts the wastewater to the reaction conditions.

그리고 본 발명은 가용화에 있는 것으로 가용화라 함은 각각의 투입된 오존산화장치, 전기산화의 반응성의 성질을 이용하여 용존 가압믹싱하여 복합부유물질의 유기물을 우선적으로 슬러지의 바이러스, 병원균 등의 세포막 즉, 박테리아 세포속의 수분과 박테리아를 분해하고 결합수 사이의 내수분을 용존산화 믹싱을 통해 분산화 물리적 파쇄로 포화된 상태에서 산화반응의 환원되는 물수화물을 통해 가수분해되는 가용화 처리인 것으로, 슬러지처리시 각종오염원 들을 산화시켜 유기물을 분해하여 감량화 하고 악취와 동반된 복합물질을 저감시켜 균질화 하는데 있다.And the present invention is in the solubilization, solubilization refers to a cell membrane of viruses, pathogens, etc. in the sludge preferentially by dissolving and pressurizing mixing using the properties of the reactivity of each input ozone oxidizing device and electro-oxidation. It is a solubilization treatment that is hydrolyzed through water hydrates reduced by oxidation reactions in a state saturated with physical crushing, decomposing water and bacteria in bacteria cells and dispersing internal water between bound water through dissolved oxidation mixing. It is aimed at homogenizing by oxidizing pollutants to decompose and reduce organic matter and to reduce complex substances accompanied with odor.

특히 본 발명은 가용화기술을 통해 유기성 폐기물의 슬러지를 가압믹싱용 교반장치에 투입시켜 오존과 전기분해를 용존탱크에서 슬러지가 산화분해 되어지도록 하여 오염부유물질과 슬러지(유기물 SS)발생량을 감량화 시킨후 무응집 방식의 통상의 탈수기를 병합시킨 농축형 데칸타와 디스크형식 원심분리기를 통해 탈수슬러지와 탈리액으로 구분되어 균질된 부유물질과 악취가 저감된 슬러지와 탈리액으로 배출된 폐수에 활성라디칼 공정을 통해 균질된 폐수농도를 조절하고, PH조정한 뒤 가압분해 분리부상조로 하여금 잔존된 미세 유기물들을 분해 및 분리시킨 후 상부 분리된 슬러리는 집수조로 이송되어 리싸이클 하고 분리된 폐수는 오존과 함께 용존탱크에 가압 믹싱 용존 미세버블 순환장치를 통해 색도, 소독, 용존 가스제어 산화반응 탈질로 균질된 폐수를 습득하고 일정한 시간을 두워 잔존되어 있는 오존처리 후 균질된 페수를 기존의 생물반응조에 연계하는 유기성 폐기물 및 폐액 균질화 병합 고도전처리를 제공하게 된다.In particular, the present invention reduces the amount of contaminated suspended matter and sludge (organic material SS) generated by introducing the sludge of organic waste into the stirring device for pressurized mixing through the solubilization technology so that the sludge is oxidatively decomposed in the dissolved tank by ozone and electrolysis. Through a concentrated decanter incorporating a non-agglomerated conventional dehydrator and a disk type centrifuge, it is divided into dehydrated sludge and dewatering liquid, and the wastewater discharged as homogeneous suspended matter and odor-reduced sludge and dewatering liquid through an activated radical process. After adjusting the concentration of the homogeneous wastewater, adjusting the pH, the pressure decomposition separation tank decomposes and separates the remaining fine organic matter, and the upper separated slurry is transferred to the collection tank for recycling, and the separated wastewater is pressurized into the dissolved tank with ozone. Organic waste and waste liquid that acquires homogeneous wastewater by controlling color, disinfection, and dissolved gas through a mixing dissolved microbubble circulation device through oxidation reaction and denitrification, and connects the homogeneous wastewater to the existing bioreactor after ozone treatment remaining for a certain period of time. Homogenization merger provides advanced pretreatment.

또한 본 발명은 고도전처리 슬러지 감량화로 배출되며, 특히 축산분뇨 자체를 처리하는 데는 악취저감 및 무응집방식으로 슬러지가 배출되어 부숙화, 퇴비화 등 자원 재활용할 가치의 발전가능한 균질된 목적물로 활용되기 위한 기존 선행 시설의 적용성 및 효율성을 극대화시키고 자원 재활용의 에너지원을 확보하며, 가장 큰 습득물은 냄새안나는 슬러지로 배출된다는 점은 현재 모든 육상에서 발생된 폐기물을 육상에서 해결해야 한다는 것으로 볼 때 각종 민원과 상생가능한 진보적인 고도전처리처리 방법을 제공하는 것이다.In addition, the present invention is discharged through the reduction of advanced pre-treatment sludge, and in particular, in order to treat livestock manure itself, sludge is discharged in a manner that reduces odor and does not coagulate, so that it can be used as a homogeneous object capable of developing the value of recycling resources such as composting and composting. The fact that the applicability and efficiency of existing pre-existing facilities is maximized, and the energy source for resource recycling is secured, and that the biggest gained product is discharged as odorless sludge, considering that all waste generated on land must be resolved on land. It is to provide an advanced and advanced pretreatment method that can coexist with

아울러 본 발명은 기존 기술들이 생물반응 구조의 바탕의 기준을 둔 기술로 사계절이 있는 우리나라에서는 참 유지관리 하기에는 한계가 있어 본 발명의 개발동기의 가장 큰 목적은 변화폭이 최소화 될 수 있게 기계와 전기적 설비장치로 하여금 생물반응 전에 악취, 부유물질, 독성물질, 난분해성, 부패성 물질, 유기물 및 기타 물질들을 최대한 감소시킬 수 있게 하였으며 그 효과는 향상시키면서 균질성이 확보된 고도전처리 공정설비를 제공하여 생물반응 처리에 균질화된 전처리의 물질이 유입되도록 한 것이다.In addition, the present invention is a technology based on the bioreaction structure, and there is a limit to true maintenance in Korea, where there are four seasons, so the main purpose of the development motivation of the present invention is mechanical and electrical equipment so that the variation width can be minimized. Before the bioreaction, it was possible to reduce odors, suspended substances, toxic substances, hardly degradable, perishable substances, organic substances, and other substances as much as possible, and improved the effect while providing a high-level pretreatment process facility that secured homogeneity for bioreaction treatment. This is to allow the homogenized pre-treatment material to flow into.

더하여 본 발명은 국내유형으로 볼 때 갈수록 규제는 강화되어만 가는데 원인적인 전처리기준을 최적화시켜 후단부분에 부하를 줄이는 특화되어 있는 설비로 구성 되었으며, 현장 적용을 통한 융합기술을 최적화 한 고도전처리 표준화 기술을 제공하여 근본적인 인식구조를 변화시킬 수 있도록 한 것이다.In addition, the present invention is composed of specialized facilities to reduce the load at the rear end by optimizing the causal pretreatment standard, although the regulations are getting stronger as it is viewed as a domestic type, and advanced pretreatment standardization technology optimized through field application It is to be able to change the fundamental recognition structure.

본 발명은 상기한 효과로 인해 고도전처리 장치의 품질과 신뢰성을 대폭 향상시키므로 사용자인 소비자들의 다양한 욕구(니즈)를 충족시켜 좋은 이미지를 심어줄 수 있도록 한 매우 유용한 발명인 것이다.The present invention is a very useful invention in which a good image can be planted by satisfying the various needs (needs) of consumers, which are users, because the quality and reliability of the advanced preprocessing device are greatly improved due to the above effects.

이하에서는 이러한 효과 달성을 위해 유기성 폐기물의 발생현장 중 가장 문제성이 시급한 가축분뇨처리 실태를 파악하고, 국내 여타조건의 선행기술의 장치들을 파이롯트 적용 테스트를 거처 융합기술을 4년간 적용 가능하면서 발전 가능한 병합 시스템을 습득 후 비 전문가도 취급 설명만으로 작동 가능한 물리적처리 시스템을 구축하기 위해 실질적인 적용가능한 낙후된 가축분뇨 농장에서 3년간 적용실시를 통한 습득된 결과물을 바탕으로, 본 발명의 바람직한 실시 예를 첨부된 도면에 따라 상세히 설명하면 다음과 같다.In the following, in order to achieve this effect, the most urgent livestock manure treatment situation among organic waste generation sites is identified, and the convergence technology can be applied for 4 years while developing possible merger through pilot application testing of devices of the prior art under other conditions in Korea. After acquiring the system, a preferred embodiment of the present invention is attached based on the results obtained through three years application practice in a practically applicable obsolete livestock manure farm in order to construct a physical processing system that can be operated only by handling explanations even by non-experts. It will be described in detail according to the drawings as follows.

도 1 은 본 발명에 적용된 유기성 폐기물 및 폐액 균질화 고도전처리 장치의
구성도.
도 2 는 본 발명에 적용된 유기성 폐기물 및 폐액 균질화 고도전처리 방법을
보인 흐름도.
도 3 은 본 발명 유기성 폐기물 처리대상물질을 처리하는 사진.
도 4 는 본 발명 집수조(혐기조운영)에서 가용화처리하는 사진.
도 5 의 (a)는 본 발명 가용화처리된 분뇨 무약주(응집제를 주입하지 않음)(무응집) 방식의 탈수슬러
리 처리사진이고,
(b)는 본 발명 가용화처리된 분뇨 무약주(응집제를 주입하지 않음)(무응집) 방식의 탈수액 처
리사진이다.
도 6 은 본 발명 탈리액(폐수) 오존장치를 통한 활성라디칼처리 사진.
도 7 은 본 발명 활성라디칼조를 거쳐 낙후되어 있는 통상적인 생물반응조를
통과 후 가압분해부상분리처리하는 사진.
도 8 은 본 발명 가압분해부상처리 후 전기분해 산화응집부상처리 사진.
1 is an organic waste and waste liquid homogenization advanced pretreatment apparatus applied to the present invention
Diagram.
Figure 2 is an organic waste and waste liquid homogenization advanced pretreatment method applied to the present invention
Flow chart shown.
Figure 3 is a photograph of processing the present invention organic waste treatment target material.
Figure 4 is a photograph of the solubilization treatment in the present invention water collecting tank (anaerobic tank operation).
Figure 5 (a) is a dehydration slur of the present invention solubilization-treated manure-free liquor (no coagulant is injected) (no coagulation) method
This is a photograph of Lee processing,
(b) is a dehydration liquid treatment of the present invention solubilized manure-free alcoholic beverage (no coagulant is injected) (no-aggregation)
This is Lisa.
Figure 6 is a photograph of the active radical treatment through the present invention desorption liquid (wastewater) ozone device.
Figure 7 shows a conventional bioreactor that is underdeveloped through the active radical tank of the present invention.
Photo of separation treatment by pressure decomposition after passing.
Figure 8 is a photograph of the electrolytic oxidation agglomeration wound treatment after the present invention pressure cracking flotation treatment.

본 발명에 적용된 유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법은 도 1 내지 도 8 에 도시된 바와 같이 구성되는 것이다.The organic waste and waste liquid homogenization advanced pretreatment apparatus and method applied to the present invention is configured as shown in FIGS. 1 to 8.

하기에서 본 발명을 설명함에 있어, 관련된 공지 기능 또는 구성에 대한 구체적인 설명이 본 발명의 요지를 불필요하게 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명은 생략할 것이다.In the following description of the present invention, if it is determined that a detailed description of a related known function or configuration may unnecessarily obscure the subject matter of the present invention, a detailed description thereof will be omitted.

그리고 후술되는 용어들은 본 발명에서의 기능을 고려하여 설정된 용어들로서 이는 생산자의 의도 또는 관례에 따라 달라질 수 있으므로 그 정의는 본 명세서 전반에 걸친 내용을 토대로 내려져야 할 것이다.In addition, terms to be described later are terms set in consideration of functions in the present invention and may vary according to the intention or custom of the producer, so the definition should be made based on the contents throughout the present specification.

또한 도면에서 나타난 각 구성의 크기 및 두께는 설명의 편의를 위해 임의로 나타내었으므로, 본 발명이 반드시 도면에 도시된 바에 한정되지 않는다.In addition, the size and thickness of each component shown in the drawings are arbitrarily shown for convenience of description, so the present invention is not necessarily limited to those shown in the drawings.

먼저, 본 발명은 융합장치의 고도전처리분리기술인 H-PDS기술(High class-Pretreatment process Division System)에 관한 것으로, 특히 오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술인 유기성 폐기물 및 폐액 균질화 고도전처리 장치에 관한 것이다.First, the present invention relates to a high class-pretreatment process division system (H-PDS) technology, which is a high-level pretreatment process division system of a fusion device, and in particular, various pollutant concentrations, pathogens, viruses, and It relates to an advanced pretreatment device for homogenizing organic waste and waste liquid, which is an advanced pretreatment technology that can reduce odor.

상기 유기성 폐기물(有機性廢棄物, organic waste) 및 폐액 균질화 고도전처리 장치는 다음과 같이 구성된다.The advanced pretreatment apparatus for homogenizing organic waste and waste liquid is configured as follows.

즉, 본 발명은 원분뇨처리시 털이나 기계가동에 부적합한 협착물질을 제거하는 유기성폐기물처리장치(100)가 구비된다.That is, the present invention is provided with an organic waste treatment apparatus 100 that removes hairs or constricting substances unsuitable for machine operation during raw manure treatment.

또한 본 발명은 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 활성라디칼 가압 가용화장치(200)가 구비된다.In addition, the present invention is provided with an activated radical pressure solubilization device 200 for inducing the separation and separation of suspended substances through stabilization and solubilization of organic waste.

그리고 본 발명은 무응집 방식의 탈수장치로 슬러지와 탈리액을 분리하는 탈수슬러지 처리장치(300)가 구비된다.In addition, the present invention is provided with a dewatering sludge treatment device 300 for separating sludge from a dewatering liquid as a dewatering device of a non-aggregation method.

또한 본 발명은 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 활성분해순환장치(400)가 구비된다.In addition, the present invention is provided with an active decomposition circulation device 400 for inducing oxidative decomposition through a free radical reaction in contact with organic wastewater of the desorption liquid.

그리고 본 발명은 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 분해부상처리장치(500)가 구비된다.In addition, the present invention is provided with a decomposition flotation treatment device 500 for decomposing and flotating the complex oxide material dissolved by the pressure decomposition flotation treatment.

마지막으로 본 발명은 가압분해 부상분리 처리 후 전기분해 산화응집침전 상등수를 마이크로버블로 부상처리하는 전기분해 산화응집침전 부상처리장치(600);가 순차적으로 연결 구비된 유기성 폐기물 및 폐액 균질화 고도전처리 장치를 제공한다.Finally, the present invention is an electrolytic oxidation coagulation and precipitation flotation treatment device 600 for flotating the supernatant of the electrolysis oxidation coagulation and precipitation in microbubbles after the flotation treatment by pressure decomposition; an advanced pretreatment device for homogenizing organic waste and waste liquid provided sequentially connected Provides.

상기한 본 발명의 보다 구체인 기술적 구성은 다음과 같다.A more specific technical configuration of the present invention is as follows.

먼저, 본 발명에 적용된 상기 유기성폐기물처리장치(100)는, 원분뇨 침전 방지용 순환교반장치(111)와 연결되는 협착물제거용 스크린(112)과, 상기 스크린(112)으로 털이나 이물질만 분리하여 집수조(113)로 공급하도록 구성된다.First, the organic waste treatment apparatus 100 applied to the present invention separates only hairs or foreign substances by the screen 112 for removing strictures connected to the circulation stirring device 111 for preventing raw manure precipitation. It is configured to be supplied to the water collecting tank 113.

이때 상기 원분뇨 침전 방지용 순환교반장치(111)는 PH 6.5이하의 밀폐된 공간의 혐기성화 순환으로 최대한 공기를 차단하고 외부로 악취유출을 억제하며, 교반펌프와 수중펌프로 일정시간 반송하여 유기태질소(organonitrogen) 즉, 유기성 물질중 질소가 유기 화합물로 존재하는 단백질 또는 그 밖의 화합물들이 산소 및 부패성 물질로 전환되어 암모니아성 질소로 전환되는 것을 억제시켜는 공정단계로 순환할 수 있도록 구성된다.At this time, the circulation agitator 111 for preventing raw manure precipitation blocks air as much as possible through anaerobic circulation in a closed space with a pH of 6.5 or less, suppresses odor leakage to the outside, and returns organic nitrogen for a certain period of time to a stirring pump and an underwater pump. (organonitrogen) In other words, it is configured to circulate to a process step that inhibits the conversion of proteins or other compounds in which nitrogen among organic substances is present as organic compounds to oxygen and perishable substances to be converted to ammonia nitrogen.

그리고 상기 협착물제거용 스크린(112)은 원분뇨처리시 털이나 각종 기계가동에 부적합한 협착물질을 제거하는 것으로, 20~30톤 원분뇨 스크린형 장치로 털털이장치 및 드럼스크린장치로 협착물을 제거한다.In addition, the screen for removing constrictions 112 removes hairs or constricting substances unsuitable for operation of various machines during raw manure treatment, and is a 20-30 ton raw manure screen-type device to remove constrictions with a hair removal device and a drum screen device. do.

또한 본 발명에 적용된 상기 활성라디칼 가압 가용화장치(200)는, 유기성폐기물처리장치(100)와 연결되며, HI-COS장치(211)를 이용하여 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도 및 축산분뇨의 유기물을 분해하여 가용화하도록 구성된다.In addition, the activated radical pressurized solubilization device 200 applied to the present invention is connected to the organic waste treatment device 100, and induces separation of suspended substances through stabilization and solubilization of organic wastes using the HI-COS device 211, and It is configured to decompose and solubilize organic matter in livestock manure.

이때 상기 HI-COS장치(211)는 원분뇨 저류조 가용화 교반 라디칼 접촉 산화장치로, 가용화 순환처리와 가용화처리수를 거쳐 400~600톤 원분뇨 악취저감 2단계 설비로 이루어진다.At this time, the HI-COS device 211 is a raw manure storage tank solubilization and agitation radical contact oxidation device, and consists of a two-stage facility for reducing odor of raw manure from 400 to 600 tons through solubilization circulation treatment and solubilization treated water.

그리고 본 발명에 적용된 상기 탈수슬러지 처리장치(300)는, 활성라디칼 가압 가용화장치(200)와 연결되며, 탈수장치(311)와 부유물질 분리장치(312)를 이용하여 가축분뇨의 탈수슬러지와 탈리액을 분리하여 탈수슬러지는 퇴비화 처리를 하도록 연계처리하며, 탈리액은 액비나 정화처리를 하도록 연계처리 구성된다.And the dewatered sludge treatment apparatus 300 applied to the present invention is connected to the activated radical pressure solubilization apparatus 200, and the dehydration sludge and dewatering liquid of livestock manure by using the dehydration apparatus 311 and the floating substance separation apparatus 312 By separating the dewatered sludge, the dewatered sludge is treated in conjunction with composting treatment, and the desorbed liquid is composed of a linkage treatment to perform liquid manure or purification treatment.

이때 상기 탈수장치(311)는 20~30톤 원분뇨를 처리할 수 있게 3단 설비로 이루어지고, 상기 부유물질 분리장치(312)는 부유물질을 분리하도록 2단계 분리장치로 이루어진다.At this time, the dehydration device 311 is made of a three-stage facility capable of processing 20 to 30 tons of raw manure, and the floating material separation device 312 is made of a two-stage separation device to separate the floating material.

또한 본 발명에 적용된 상기 활성분해순환장치(400)는, 탈수슬러지 처리장치(300)와 연결되며, 오존(O3)발생장치(411)와 활성라디칼산화장치(412)를 이용하여 탈리액의 유기성폐수와 접촉 자유라디칼 반응으로 산화분해 유도하도록 구성된다.In addition, the active decomposition circulation device 400 applied to the present invention is connected to the dewatered sludge treatment device 300, and uses an ozone (O3) generating device 411 and an activated radical oxidizing device 412 to form organic wastewater of the stripping liquid. It is configured to induce oxidative decomposition as a free radical reaction in contact with.

이때 상기 오존(O3)발생장치(411)와 활성라디칼산화장치(412)는 탈리액(폐수)를 오존장치를 통한 OH-활성라디칼을 처리하도록 분리장치는 4단계로 이루어지고, 악취 및 미세부유물질을 저감할 수 있게 2단 순환처리 설비로 이루어진다.At this time, the ozone (O3) generating device 411 and the active radical oxidizing device 412 are separated by four steps so as to treat OH-active radicals through an ozone device with a desorbing liquid (wastewater), and It consists of a two-stage circulation treatment facility to reduce

그리고 본 발명에 적용된 상기 분해부상처리장치(500)는, 활성분해순환장치(400)와 연결되며, 생물학적처리장치(511)와 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 부상분리처리장치(512)를 이용하여 처리하도록 구성된다.And the decomposition flotation treatment device 500 applied to the present invention is connected to the active decomposition circulation device 400, the biological treatment device 511 and the flotation treatment device for complex oxides dissolved in the flotation treatment under pressure It is configured to process using 512.

이때 본 발명은 상기 생물학적처리장치(511)와 가압분해 부상분리처리를 거친 후 부상분리처리장치(512)를 이용하여 1,2차 부상처리할 수 있도록 한다.At this time, the present invention allows the first and second flotation treatments to be performed using the flotation treatment device 512 after the biological treatment device 511 and the pressure decomposition flotation treatment are performed.

또한 본 발명에 적용된 상기 전기분해 산화응집 부상처리장치(600)는, 분해부상처리장치(500)와 연결되며, 용해성 콜로이드입자 전과 후 처리로 오존산화 미세버블 및 전기분해 산화응집 침전 상등수를 부상 마이크로 버블처리로 난분해성 물질과 색도분해를 유도하도록 구성된다.In addition, the electrolysis oxidative agglomeration flotation treatment apparatus 600 applied to the present invention is connected to the decomposition flotation treatment device 500, and microbubbles of ozone oxidation and electrolysis oxidative agglomeration precipitation supernatant water are floated before and after soluble colloid particles. It is constructed to induce decomposable material and chromaticity decomposition by bubble treatment.

이때 상기 전기분해 산화응집 침전 및 부상처리장치(600)는 전기분해 응집침전과 상등수를 가압분해 부상분리처리 그리고 전기분해 적용을 거쳐 정화시키게 된다.At this time, the electrolytic oxidation coagulation precipitation and flotation treatment device 600 purifies the electrolytic coagulation precipitation and supernatant water through pressure decomposition flotation separation treatment and electrolysis application.

한편 본 발명은 상기의 구성부를 적용함에 있어 다양하게 변형될 수 있고 여러 가지 형태를 취할 수 있다.On the other hand, the present invention can be variously modified and take various forms in applying the above-described components.

그리고 본 발명은 상기의 상세한 설명에서 언급되는 특별한 형태로 한정되는 것이 아닌 것으로 이해되어야 하며, 오히려 첨부된 청구범위에 의해 정의되는 본 발명의 정신과 범위 내에 있는 모든 변형물과 균등물 및 대체물을 포함하는 것으로 이해되어야 한다.And it should be understood that the present invention is not limited to the particular form mentioned in the detailed description above, but rather, including all modifications and equivalents and substitutes within the spirit and scope of the present invention as defined by the appended claims. It should be understood as.

상기와 같이 구성된 본 발명 유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법의 작용효과를 설명하면 다음과 같다.The operation and effect of the apparatus and method for homogenizing organic waste and waste liquid of the present invention configured as described above will be described as follows.

우선, 본 발명은 오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술을 제공하는 것이다.First, the present invention provides a fusion/complex advanced pretreatment technology capable of reducing the concentration of various pollutants, pathogens, viruses, and odors before being separated into organic waste and wastewater having a high pollutant concentration.

본 발명의 작용 효과를 설명하기에 앞서 도 1 은 본 발명에 적용된 유기성 폐기물 및 폐액 균질화 고도전처리 장치의 구성도이다.Prior to describing the effects of the present invention, FIG. 1 is a block diagram of an advanced pretreatment apparatus for homogenizing organic waste and waste liquid applied to the present invention.

그리고 도 2 는 본 발명에 적용된 유기성 폐기물 및 폐액 균질화 고도전처리 방법을 보인 흐름도이다.And Figure 2 is a flow chart showing the organic waste and waste liquid homogenization advanced pretreatment method applied to the present invention.

상기한 기술적 흐름도는 유기성 폐기물 및 폐액 균질화 고도전처리 장치를 이용한 유기성 폐기물 및 폐액 균질화 고도전처리 방법에 관한 것으로, 유기성 폐기물 처리대상물질을 협착물제거용 스크린(112)을 이용하여 털이나 이물질만을 분리하여 집수조(113)로 공급하는 단계(S10)를 거친다.The above technical flow chart relates to a method of advanced pretreatment for organic waste and waste liquid homogenization using an advanced pretreatment device for organic waste and waste liquid homogenization, by separating only hairs or foreign substances by using a screen 112 for removing constrictions It goes through the step (S10) of supplying to the water collecting tank (113).

이후 본 발명은 축산분뇨의 유기물을 분해하여 가용화하는 활성라디칼 가압 가용화장치(200)를 이용하여 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 단계(S20)를 거친다.Thereafter, the present invention undergoes a step (S20) of stabilizing organic waste and inducing the separation of suspended matter through solubilization using an activated radical pressure solubilization device 200 that decomposes and solubilizes organic matter in livestock manure.

이어서 본 발명은 가용화처리된 분뇨 무약주(무응집: 응집제를 주입하지 않음) 탈수슬러지 처리장치(300)를 이용하여 슬러지와 탈리액을 분리하는 단계(S30)를 거친다.Subsequently, the present invention undergoes a step (S30) of separating the sludge from the dewatering liquid using the dehydrated sludge treatment device 300 (no coagulation: no coagulant is injected) solubilized.

이후 본 발명은 오존발생장치(411)가 포함된 활성분해순환장치(400)를 이용하여 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 단계(S40)를 거친다.Thereafter, the present invention undergoes a step (S40) of inducing oxidative decomposition through a contact free radical reaction with organic wastewater of the desorption liquid using the active decomposition circulator 400 including the ozone generator 411.

이어서 본 발명은 분해부상처리장치(500)를 이용하여 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 단계(S50)를 거친다.Subsequently, the present invention undergoes a step (S50) of decomposing and treating the dissolved complex oxide material by the pressure decomposition flotation treatment using the decomposition flotation treatment apparatus 500.

이후 본 발명은 전기분해 산화응집침전 부상처리장치(600)를 이용하여 유기성 폐기물 특성에 따라 복합 또는 개별장치로 용해성 콜로이드입자 전과 후처리로 오존산화 미세버블 및 전기분해 산화 응집부상 마이크로 버블처리로 난분해성 물질과 색도분해유도하는 단계(S60)거쳐서 유기성 폐기물 및 폐액 균질화 고도전처리 방법을 제공한다.Thereafter, the present invention uses the electrolytic oxidative coagulation flotation treatment device 600 to treat soluble colloid particles before and after treatment in a complex or separate device according to the characteristics of organic waste. It provides an advanced pretreatment method for homogenizing organic waste and waste liquid through the step (S60) of inducing degradable material and chromaticity decomposition.

상기한 본 발명을 수행하기 위해 본 발명에 적용된 도 3 은 유기성 폐기물 처리대상물질을 처리하는 사진이다.Figure 3 applied to the present invention in order to carry out the present invention described above is a photograph of processing an organic waste treatment target material.

즉, 상기한 본 발명은 원분뇨침전방지용 순환교반장치(111)가 혐기성 순환으로 최대한 공기를 차단하고 외부로 악취유출을 억제하여 교반펌프를 이용하여 스크린(112)으로 이송하면 스크린(112)은 축산분뇨의 이물질을 협착물 제거용으로 폐기물을 처리함에 있어, 파쇄, 파봉, 협착물제거는 기본설비로 축산분뇨를 처리하고, 털이나 이물질만 분리하여 집수조(113)로 보내지는 것으로, 축산분뇨를 원활하게 펌프로 이송하는 것이다.That is, in the present invention, when the circulation stirring device 111 for preventing raw manure precipitation is transferred to the screen 112 using an agitating pump by blocking air as much as possible through anaerobic circulation and suppressing the outflow of odor to the outside, the screen 112 is In processing waste for removing foreign substances from livestock manure, crushing, crushing, and removing strictures are basic facilities to treat livestock manure, and separate only hairs or foreign substances and send them to the collection tank 113. Is smoothly transferred to the pump.

상기한 결과 본 발명은 아래 표 1 과 같은 시험결과를 얻게 되었다.As a result of the above, the present invention obtained the test results shown in Table 1 below.

Figure 112020025481310-pat00001
Figure 112020025481310-pat00001

본 발명은 상기한 시험 결과 통상적인 스크린통과 처리시 부유물질, BOD, CODMN, CODCR, 총질소, 암모니아성질소, 총인이 소폭 감소되었고, PH는 혐기성 운전이 되었음을 확인할 수 있다.As a result of the above-described test, it can be seen that suspended matter, BOD, COD MN , COD CR, total nitrogen, ammonia nitrogen, and total phosphorus were slightly reduced, and the pH became anaerobic during normal screen passing treatment.

도 4 는 HI-C.O.S (High-Circulation Ohradical process System)으로, 집수조(혐기조운영)에서 가용화처리하는 사진이다.4 is a photograph of a solubilization treatment in a water collecting tank (anaerobic tank operation) with HI-C.O.S (High-Circulation Ohradical Process System).

즉, 상기한 본 발명은 축산분뇨의 유기물을 분해하여 가용화하는 설비로 통상적인 오존산화 및 전기산화 장치의 특성을 이용해 가압탱크에서 가압과 교반 믹싱으로 분뇨를 가용화 가수분해 함과 동시에 부폐성 유기물을 저감하는 가압순환 가용화처리 시스템이다.That is, the present invention is a facility that decomposes and solubilizes organic matter in livestock manure. Using the characteristics of conventional ozonation and electrooxidation equipment, the manure is solubilized and hydrolyzed by pressing and stirring mixing in a pressurized tank, and at the same time, waste organic matter is removed. It is a reduced pressure circulation solubilization treatment system.

특히 순환가용화 시스템을 통해 분뇨의 유기물과 복합 부유물질 농도 저감을 1차적으로 균질화시키는 기본 단계이다.In particular, it is the basic step of homogenizing the concentration of organic matter and complex suspended matter in manure through the circulation solubilization system.

상기한 결과 본 발명은 아래 표 2 과 같은 시험결과를 얻게 되었다.As a result of the above, the present invention obtained the test results shown in Table 2 below.

Figure 112020025481310-pat00002
Figure 112020025481310-pat00002

본 발명은 상기한 시험 결과 스크린부유물질, BOD, CODMN, CODCR, 총질소, 암모니아성질소, 총인이 감소되었고, PH는 혐기성 운전이 되었음을 확인할 수 있다.In the present invention, as a result of the above test, it can be confirmed that the screen floating material, BOD, COD MN , COD CR, total nitrogen, ammonia nitrogen, and total phosphorus were reduced, and that the PH became anaerobic operation.

도 5 는 O.D.S (Original process Decanter Sludse system)으로, (a)는 본 발명 가용화처리된 분뇨 무약주(무응집: 응집제를 주입하지 않음) 방식의 탈수슬러리 처리사진이고, (b)는 본 발명 가용화처리된 분뇨 무약주(무응집; 응집제를 주입하지 않음) 방식의 탈수액 처리사진이다.5 is an ODS (Original Process Decanter Sludse system), (a) is a photograph of dehydrated slurry treatment of the present invention solubilization-treated manure-free alcoholic beverage (no aggregation: no coagulant is injected), and (b) is the present invention solubilization This is a picture of the dehydration liquid treatment of the treated manure-free liquor (no agglomeration; no coagulant is injected).

즉, 일반적으로 모든 유기성 폐기물 고도전처리공정은 크게 두가지로 구분되어 탈수슬러지분리공정과 탈리액분리공정으로 분리되어 처리된다.That is, in general, all advanced pretreatment processes for organic wastes are largely divided into two, and are separated into a dewatered sludge separation process and a stripping liquid separation process.

통상적으로 가축분뇨처리 기존의 전처리과정은 폐기물을 분리하기 위해 고분자응집제를 첨가하여 폐기물을 탈수 분리하였지만 이러한 화학적 첨가제로 하여금 빠른 효과와 폐기물 및 폐수를 분리할 수 있었지만 이차적 분해가 어려운 폴리머 성분 때문에 가축분뇨의 탈리된 분뇨슬러지가 부숙화되는데 상당한 시간이 걸린다.Conventionally, livestock manure treatment The existing pretreatment process dehydrated and separated waste by adding a polymer coagulant to separate the waste, but these chemical additives were able to separate waste and wastewater with a quick effect, but because of the polymer component that is difficult to secondary decomposition, livestock manure It takes a considerable time for the desorbed manure sludge to become compostable.

또한 생물학적 처리시 가축분뇨의 발생과정 중 과다한 항생제와 고분자 응집제의 폴리머 성분 때문에 갈수록 생물학적 분해가 어렵고 부하농도가 높아저 결국 생물학적 처리시설을 증설해야하는 문제점을 않고 있다.In addition, during the biological treatment, due to excessive antibiotics and polymer components of the polymer coagulant during the generation of livestock manure, biological decomposition is increasingly difficult and the load concentration is high, so there is no problem of increasing biological treatment facilities.

본 발명의 개념(매카니즘)ODS 탈수시스템은(무응집: 응집제를 주입하지 않음) 가축분뇨의 탈수슬러지와 탈리액을 분리하여 탈수슬러지는 퇴비화 처리를 하도록 연계처리 하며, 탈리액은 액비나 정화처리를 하도록 연계처리를 하는데 있다.Concept (mechanism) of the present invention The ODS dewatering system (no coagulation: no coagulant is injected) separates the dehydrated sludge and the depleted liquid of livestock manure, so that the dewatered sludge is subjected to composting treatment, and the dewatering liquid is used for liquid manure or purification treatment. It is in connection processing.

특히 앞공정의 HI-COS시스템을 통해 축산분뇨의 유기물을 분해 배출된 분뇨 슬러지는 악취냄새가 극감되었으며, 분뇨슬러지는 통상적인 슬러지와 달리 미세된 슬러지로 분리 표면적이 극되화 되어 빠른 부숙화, 건조효율, 부숙시설이 냄새 저감으로 인한 취급 용이성이 탁월함을 알 수 있었다.In particular, through the HI-COS system in the preceding process, the odor of the manure sludge that was decomposed and discharged from the livestock manure was dramatically reduced, and the manure sludge was separated into fine sludge, unlike conventional sludge, and the surface area became extremely extreme, resulting in rapid maturation and drying. It was found that the efficiency and the ease of handling due to the reduction of odor in the incoming facilities were excellent.

또한 앞공정의 HI-COS시스템을 통해 축산분뇨의 유기물을 분해로 배출된 탈리액은(혐기성 운전과 가용화처리를 통한 유기물 분해로 유기태질소는 감소되었고 분리화된 탈리액으로 암모니아성 질소는 안정화된 상태) 기존의 폭기(공기) 및 순환장치, 기타 기존 효율장치에 효과가 극대화 되면서 균질적인 탈리액(폐수)를 처리할 수 있게 부유물의 농도는 저감시키며, 유해가스물질들은 안정화시킨다.In addition, the decomposition liquid discharged through decomposition of organic matter in livestock manure through the HI-COS system in the preceding process (organic nitrogen was reduced by decomposition of organic matter through anaerobic operation and solubilization treatment, and ammonia nitrogen was stabilized with the separated desorption liquid) While the effect is maximized in the existing aeration (air) and circulation devices, and other existing efficiency devices, the concentration of suspended matter is reduced so that the homogeneous desorption liquid (wastewater) can be treated, and harmful gaseous substances are stabilized.

본 발명은 아래 표 3 과 같은 실험결과를 통하여 입증된 것으로 유기성물질의 저감과 질소 안정화상태로(암모니아성질소와 총질소 값이 비슷하게 나올 때 폐수에 존재하는 유기태질소는 분해되어 총 질소값이 저감한 혐기 분리화된 탈리액 폐수) 다음 공정의 생물학적처리 또는 공기폭기 및 기타 효율성 장치에 최적화 반응되도록 질산화, 탈질화, 액비화, 정화처리가 극대화된 반응이 가능하도록 구성되었다.The present invention was proved through the experimental results shown in Table 3 below, and in a state of reduction of organic substances and nitrogen stabilization (when the values of ammonia nitrogen and total nitrogen are similar, organic nitrogen present in the wastewater is decomposed and the total nitrogen value is reduced. It is configured to maximize the reaction of nitrification, denitrification, liquefaction, and purification so as to react optimally to the biological treatment of the next process or air aeration and other efficiency devices.

Figure 112020025481310-pat00003
Figure 112020025481310-pat00003

본 발명은 상기한 시험 결과 유기물 분해를 통한 부유물질과 총질소는 감소되었으며, 총질소와 암모니아성질소가 점점 비슷해지는 것을 확인할 수 있다.In the present invention, as a result of the above test, it can be seen that suspended matter and total nitrogen are reduced through decomposition of organic matter, and total nitrogen and ammonia nitrogen are gradually becoming similar.

본 발명 상기 슬러지와 탈리액을 분리하는 단계(S30)는, 가축분뇨의 탈수슬러지와 탈리액을 분리하여 탈수슬러지는 퇴비화처리를 하도록 연계처리하며, 탈리액은 액비나 정화처리를 하도록 연계처리를 할 수 있음은 물론이다.In the present invention, the step of separating the sludge and the desorption liquid (S30), the dewatered sludge of livestock manure and the dewatering liquid are separated, and the dewatered sludge is treated to be composted, and the desorption liquid can be linked to liquid manure or purification treatment. Of course.

도 6 은 OH-활성라디칼(OH-radical process system)로, 본 발명 탈리액(폐수) 오존장치를 통한 활성라디칼처리 사진이다.6 is an OH-active radical (OH-radical process system), which is a photograph of an active radical treatment through the present invention desorption liquid (wastewater) ozone device.

상기한 본 발명 OH- 활성라디칼 순환처리 시스템은 탈리액(폐수) 상위결과를 볼 때 질소농도가 높아 기존 생물 반응조 기반 폭기를 할 경우 암모니아성 질소가 질산화되어 무산소 조건의 탈질부하 즉, NO2, NO3의 근본적인 질소 처리에 문제가 있어 오존처리를 하여금 오염 폐수와 접촉시켜 가압 순환처리를 통해 OH 활성라디칼반응(프리라디칼,오존산화반응,기타 오염물질 분해 반응을 통한 자유활성라디칼 산화반응)으로 황화수소 H2S, 암모니아 NH3 등의 기타 오염물들을 최대한 저감화시켜 액비화 및 정화처리를 하도록 연계처리를 하는데 있다.The above-described OH-activated radical circulation treatment system of the present invention has a high nitrogen concentration when looking at the upper result of the elimination liquid (wastewater), and ammonia nitrogen is nitrified when aeration based on the existing biological reactor is performed. Since there is a problem with the fundamental nitrogen treatment, the ozone treatment is brought into contact with contaminated wastewater, and OH active radical reaction (free radical oxidation reaction through free radical, ozone oxidation, and other contaminant decomposition reactions), hydrogen sulfide H2S It is to conduct a linkage treatment to liquefy and purify by reducing other pollutants such as ammonia, NH3, etc. as much as possible.

특히 앞공정의 HI-COS시스템 + ODS 탈수시스템 통합형 가축분뇨 분리장치 시스템을 통해 축산분뇨의 유기물을 분해로 배출된 탈리액은(혐기분리화된 탈리액으로 질소고정 안정화된 상태 )기존의 폭기(공기) 및 순환장치, 기타 기존 효율장치에 효과가 극대화 되면서 균질적인 탈리액(폐수)를 처리할 수 있는 부유물의 농도를 저감하게 되었으며, 유해가스물질들이 안정화되어 OH- 활성라디칼 순환처리 시스템에서 질소와 부유물질들을 극감소하게 되었다.In particular, the desorption liquid discharged from the decomposition of the organic matter of livestock manure through the HI-COS system + ODS dehydration system of the preceding process through the integrated livestock manure separation system system (a state of nitrogen fixation and stabilization with an anaerobic separation liquid) is conventional aeration (air). The concentration of suspended matter that can treat homogeneous desorption liquid (wastewater) is reduced while maximizing the effect on the circulation device and other existing efficiency devices, and nitrogen and suspended matter in the OH-activated radical circulation treatment system due to stabilization of harmful gas substances. The hearing was dramatically reduced.

상기한 수질검사결과 아래 표 4 와 같은 시험결과를 얻게 되었다.As a result of the above water quality test, the test results shown in Table 4 below were obtained.

Figure 112020025481310-pat00004
Figure 112020025481310-pat00004

그리고 O3를 활용한 OH 활성라디칼 순환 오염물질과 산화반응은 아래 화학식 1과 같은 산화반응 예식을 통해 극감된 것으로 보아진다.And it is believed that the oxidation reaction with the OH activated radical circulation pollutant using O3 was dramatically reduced through the oxidation reaction example as shown in Formula 1 below.

Figure 112020025481310-pat00005
Figure 112020025481310-pat00005

한편, 본 발명에 적용된 상기 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 단계(S40)는, 오존발생장치(411)와 활성라디칼산화장치(412)를 이용하여 활성라디칼을 1차, 2차 분해하여 탈리액의 유기성폐수와 접촉 자유라디칼 반응으로 산화분해유도할 수 있음은 물론이다.On the other hand, the step (S40) of inducing oxidative decomposition through a free radical reaction in contact with the organic wastewater of the desorption liquid applied in the present invention uses an ozone generator 411 and an active radical oxidation device 412 to primary, Of course, it is possible to induce oxidative decomposition by secondary decomposition and contact free radical reaction with organic wastewater of the desorption liquid.

도 7 은 분리 시스템(Division System)으로, 본 발명 활성라디칼조를 거쳐 낙후되어 있는 통상적인 생물반응조를 통과 후 가압분해 부상분리처리하는 사진이다.7 is a photograph of a division system, which undergoes pressurized decomposition flotation treatment after passing through a conventional bioreactor that is underdeveloped through an active radical tank of the present invention.

상기한 본 발명은 OH- 활성라디칼 순환처리 시스템을 통과하여 통상적인 생물반응조 거친 후 가압분해 부상분리처리를 통해 오염물들을 최대한 저감화시켜 액비나 정화처리를 하도록 연계처리를 하는데 있다.The present invention described above is to pass through an OH-activated radical circulation treatment system, pass through a conventional bioreactor, and then perform a linked treatment to reduce contaminants as much as possible through pressure decomposition flotation treatment to perform liquid manure or purification treatment.

상기한 결과 본 발명은 아래 표 5 와 같은 시험결과를 얻게 되었다.As a result of the above, the present invention obtained the test results shown in Table 5 below.

Figure 112020025481310-pat00006
Figure 112020025481310-pat00006

상기한 시험결과도 축산폐수의 활성라디칼조 처리수의 수치가 적합하다는 판정을 받았다.The above test result was also judged that the numerical value of the activated radical treated water of livestock wastewater was appropriate.

도 8 은 H-PDS기술(High class - Pretreatment process Division System)로서, 본 발명 가압분해부상처리 후 전기분해 산화응집부상처리 사진이다.8 is an H-PDS technology (High class-Pretreatment Process Division System), which is a photograph of the electrolysis oxidation agglomeration injury treatment after the pressure cracking injury treatment according to the present invention.

상기한 본 발명은 가압분해 부상분리처리 공정에 전기분해를 통한 난분해성물질과 정화처리 가능성을 검토하기 위해 전기분해 산화응집 침전 상등수이며, The present invention described above is a supernatant for electrolysis oxidation agglomeration and precipitation in order to examine the possibility of purification treatment and non-degradable substances through electrolysis in the pressure cracking flotation treatment process,

그 결과를 볼 때 표 6 과 같이 정화처리 또한 가능할 것으로 보아진다.Looking at the results, it is believed that purification treatment is also possible as shown in Table 6.

Figure 112020025481310-pat00007
Figure 112020025481310-pat00007

상기 전기분해를 활용한 OH활성라디칼 순환 오염물질과 산화(다음과 같이 산화반응 예식을 통해 극감된 것으로 보아진다.) 과정은 반응 챔버내에 있는 전극에 강력한 전기장을 걸어주면서 시작된다. 전류는 전극을 극성화시키기 금속이온을 용해시키고 동시에 전기분해를 통해 수산화 이온을 만들어 낸다.(아래 화학식 2)The OH-activated radical circulation pollutant and oxidation process using the electrolysis (which is considered to be dramatically reduced through the following oxidation reaction equation) begins by applying a strong electric field to the electrode in the reaction chamber. Electric current dissolves metal ions to polarize the electrode and simultaneously produces hydroxide ions through electrolysis (Formula 2 below).

Figure 112020025481310-pat00008
Figure 112020025481310-pat00008

이러한 활성이온들이 반응하여 pH 범위에 따라 침전과 함께 다양한 OH 활성라디칼 형태의 수산화철이온 중간체를 형성하게 되어지며, 형성되는 종류들은,These active ions react and precipitate according to the pH range to form an intermediate of iron hydroxide ions in the form of various OH active radicals.

FeOH2+, Fe(OH)2+, Fe2(OH)24+,Fe(OH)4-, Fe(H2O)2+, Fe(H2O)5OH2+, Fe(H2O)4(OH)2+, Fe(H2O)8(OH)24+, Fe2(H2O)6(OH)42+ 예로 형성된다.FeOH2+, Fe(OH)2+, Fe2(OH)24+,Fe(OH)4-, Fe(H2O)2+, Fe(H2O)5OH2+, Fe(H2O)4(OH)2+, Fe(H2O) )8(OH)24+, Fe2(H2O)6(OH)42+ examples.

반응식은 아래 화학식 3 과 같다.The reaction formula is shown in Formula 3 below.

Figure 112020025481310-pat00009
Figure 112020025481310-pat00009

궁극적으로는 상기 다양한 형태의 이온들은 빠르게 안정한 형태의 수산화철 - Fe(OH)3로 변환되며 침전 및 유입된 폐수내의 오염원들과 강하게 반응 난분해성 물질과 질소산화물질을 저감시킨다.Ultimately, the various types of ions are rapidly converted into stable forms of iron hydroxide-Fe(OH) 3 and react strongly with pollutants in the precipitated and introduced wastewater, reducing refractory substances and nitrogen oxides.

본 발명 유기성 폐기물 및 폐액 균질화 고도전처리 장치 및 방법의 기술적 사상은 실제로 동일결과를 반복 실시 가능한 것으로, 특히 이와 같은 본원발명을 실시함으로써 기술발전을 촉진하여 산업발전에 이바지할 수 있어 보호할 가치가 충분히 있다.The technical idea of the apparatus and method for homogenizing organic waste and waste liquid of the present invention is that it is possible to repeatedly implement the same results. In particular, by implementing the present invention, it is possible to contribute to industrial development by promoting technological development, so it is worth protecting. have.

<도면의 주요 부분에 대한 부호의 설명>
100: 유기성폐기물처리장치
200: 활성라디칼 가압 가용화장치
300: 탈수슬러지 처리장치
400: 활성분해순환장치
500: 분해부상처리장치
600: 전기분해 산화응집 부상처리장치
<Explanation of symbols for major parts of drawings>
100: organic waste treatment device
200: activated radical pressure solubilization device
300: dewatered sludge treatment device
400: active decomposition circulation device
500: decomposition wound treatment device
600: electrolysis oxidative aggregation flotation treatment device

Claims (5)

오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술인 유기성 폐기물 및 폐액 균질화 고도전처리 장치에 관한 것으로, 상기 유기성 폐기물 및 폐액 균질화 고도전처리 장치는, 원분뇨처리시 털이나 기계가동에 부적합한 협착물질을 제거하는 유기성폐기물처리장치(100)와, 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 활성라디칼 가압 가용화장치(200)와, 무응집 방식의 탈수장치로 슬러지와 탈리액을 분리하는 탈수슬러지 처리장치(300)와, 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 활성분해순환장치(400)와, 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 분해부상처리장치(500)와, 가압분해 부상분리 처리 후 전기분해 산화응집침전 상등수를 마이크로버블로 부상처리하는 전기분해 산화응집침전 부상처리장치(600);가 순차적으로 연결 포함되되,
상기 유기성폐기물처리장치(100)는, 원분뇨 침전 방지용 순환교반장치(111)와 연결되는 협착물제거용 스크린(112)과, 상기 스크린(112)으로 털이나 이물질만 분리하여 집수조(113)로 공급하도록 구성하고, 상기 원분뇨 침전 방지용 순환교반장치(111)는 PH 6.5이하의 밀폐된 공간의 혐기성화 순환으로 공기를 차단하고 외부로 악취유출을 억제하되, 교반펌프와 수중펌프로 반송하여 유기태질소(organonitrogen) 즉 유기성 물질중 질소가 유기 화합물로 존재하는 단백질과 화합물이 산소 및 부패성 물질로 전환되어 암모니아성 질소로 전환되는 것을 억제시키고, 상기 협착물제거용 스크린(112)은 원분뇨처리시 털이나 기계가동에 부적합한 협착물질을 제거하는 것으로, 20~30톤 원분뇨 스크린형 장치로 털털이장치 및 드럼스크린장치로 협착물을 제거하고,
상기 활성라디칼 가압 가용화장치(200)는, 유기성폐기물처리장치(100)와 연결되며, HI-COS장치(211)를 이용하여 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도 및 축산분뇨의 유기물을 분해하여 가용화하도록 구성하되, 상기 HI-COS장치(211)는 원분뇨 저류조 가용화 교반 라디칼 접촉 산화장치로, 가용화 순환처리와 가용화처리수를 거쳐 400~600톤 원분뇨 악취저감 2단계 설비로 이루어지고,
상기 탈수슬러지 처리장치(300)는, 활성라디칼 가압 가용화장치(200)와 연결되며, 탈수장치(311)와 부유물질 분리장치(312)를 이용하여 가축분뇨의 탈수슬러지와 탈리액을 분리하여 탈수슬러지는 퇴비화 처리를 하도록 연계처리하며, 탈리액은 액비나 정화처리를 하도록 연계처리 구성되고,
상기 활성분해순환장치(400)는, 탈수슬러지 처리장치(300)와 연결되며, 오존(O3)발생장치(411)와 활성라디칼산화장치(412)를 이용하여 탈리액의 유기성폐수와 접촉 자유라디칼 반응으로 산화분해 유도하도록 구성되고,
상기 분해부상처리장치(500)는, 활성분해순환장치(400)와 연결되며, 생물학적처리장치(511)와 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 부상분리처리장치(512)를 이용하여 처리하도록 구성되고,
상기 전기분해 산화응집침전 부상처리장치(600)는, 분해부상처리장치(500)와 연결되며, 용해성 콜로이드입자 전과 후 처리로 오존산화 미세버블 및 전기분해 산화응집침전 상등수를 부상 마이크로 버블처리로 난분해성 물질과 색도분해를 유도하도록 구성함을 특징으로 하는 유기성 폐기물 및 폐액 균질화 고도전처리 장치.
It relates to an advanced pretreatment device for organic waste and waste liquid homogenization, which is a fusion/complex advanced pretreatment technology capable of reducing the concentration of various pollutants, pathogens, viruses, and odors before being separated into organic waste and wastewater with high pollutant concentration, and homogenizing the organic waste and waste liquid The advanced pretreatment device includes an organic waste treatment device 100 that removes hairs or confining substances unsuitable for machine operation during raw manure treatment, and an active radical pressure solubilization device 200 that induces separation of suspended substances through stabilization and solubilization of organic waste. Wow, a dewatering sludge treatment device 300 that separates sludge from a dewatering liquid with a non-aggregation dehydration device, an active decomposition circulation device 400 that induces oxidation and decomposition through a free radical reaction in contact with the organic wastewater of the desorption liquid, and pressurized decomposition floatation. A decomposition flotation treatment device 500 for decomposing and flotation treatment of dissolved complex oxides by separation treatment, and an electrolysis oxidative coagulation and precipitation flotation treatment device for flotating supernatant water into microbubbles after pressure decomposition flotation treatment (600); is included sequentially connected,
The organic waste treatment device 100 includes a screen 112 for removing constrictions connected to the circulation agitating device 111 for preventing the precipitation of raw manure, and the screen 112 to separate only hairs or foreign substances to a water collecting tank 113. It is configured to supply, and the circulation stirring device 111 for preventing the precipitation of raw manure blocks air by anaerobic circulation in a closed space with a pH of 6.5 or less and suppresses the outflow of odor to the outside, but returns it to the stirring pump and the underwater pump to Nitrogen (organonitrogen), that is, proteins and compounds in which nitrogen among organic substances are present as organic compounds are converted into oxygen and perishable substances to suppress the conversion to ammonia nitrogen, and the screen 112 for removing strictures is used when processing raw manure. It is to remove hairs or constriction substances unsuitable for machine operation.It is a 20-30 ton raw manure screen-type device that removes constrictions with a hair removal device and a drum screen device.
The activated radical pressure solubilization device 200 is connected to the organic waste treatment device 100, and the HI-COS device 211 is used to stabilize and solubilize the organic waste to induce the separation of suspended substances and organic matter in livestock manure. It is configured to disassemble and solubilize, The HI-COS device 211 is a raw manure storage tank solubilization agitation radical contact oxidation device, consisting of a two-stage facility for reducing odor of 400 to 600 tons of raw manure through solubilization circulation treatment and solubilization treated water,
The dewatered sludge treatment device 300 is connected to the activated radical pressure solubilization device 200, and the dewatered sludge of livestock manure and the dewatering liquid are separated by using the dewatering device 311 and the floating material separating device 312. Is linked to compost treatment, and the desorption liquid is linked to liquid manure or purification treatment,
The active decomposition circulation device 400 is connected to the dewatered sludge treatment device 300, and a free radical reaction in contact with the organic wastewater of the desorption liquid using the ozone (O3) generator 411 and the activated radical oxidation device 412 Is configured to induce oxidative decomposition,
The decomposition flotation treatment device 500 is connected to an active decomposition circulation device 400, and uses a flotation treatment device 512 for the complex oxide material dissolved in the biological treatment device 511 and the pressure-decomposition flotation treatment. Is configured to handle,
The electrolytic oxidative coagulation and precipitation flotation treatment device 600 is connected to the decomposition flotation treatment device 500, and the ozone-oxidized microbubbles and electrolytic oxidative coagulation and precipitation supernatant are treated before and after soluble colloid particles by flotation microbubble treatment. Organic waste and waste liquid homogenization advanced pretreatment device, characterized in that it is configured to induce degradable substances and chromatic decomposition.
삭제delete 청구항 1 의 오염농도가 높은 유기성 폐기물과 폐수로 분리되기 전에 각종 오염원 농도, 병원균, 바이러스 및 악취를 저감시킬 수 있는 융·복합 고도전처리 기술인 유기성 폐기물 및 폐액 균질화 고도전처리 장치를 이용한 유기성 폐기물 및 폐액 균질화 고도전처리 방법에 관한 것으로,
유기성 폐기물 처리대상물질을 협착물제거용 스크린(112)을 이용하여 털이나 이물질만을 분리하여 집수조(113)로 공급하는 단계(S10);
상기 단계(S10)는 원분뇨침전방지용 순환교반장치(111)가 혐기성 순환으로 공기를 차단하고 외부로 악취유출을 억제하여 교반펌프를 이용하여 스크린(112)으로 이송하면 스크린(112)은 축산분뇨의 이물질을 협착물 제거용으로 폐기물을 처리함에 있어, 파쇄, 파봉, 협착물제거는 기본설비로 축산분뇨를 처리하고, 털이나 이물질만 분리하여 집수조(113)로 보내지는 것으로, 축산분뇨를 원활하게 펌프로 이송하고,
이후 축산분뇨의 유기물을 분해하여 가용화하는 활성라디칼 가압 가용화장치(200)를 이용하여 유기성폐기물 안정화 및 가용화를 통한 부유물질 분리화유도하는 단계(S20);
이어서 가용화처리된 분뇨 무약주(무응집: 응집제를 주입하지 않음) 탈수슬러지 처리장치(300)를 이용하여 슬러지와 탈리액을 분리하는 단계(S30);
이후 오존발생장치(411)가 포함된 활성분해순환장치(400)를 이용하여 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 단계(S40);
이어서 분해부상처리장치(500)를 이용하여 가압분해 부상분리처리로 용존되어 있는 복합산화물질을 분해부상처리하는 단계(S50);
이후 전기분해 산화응집침전 부상처리장치(600)를 이용하여 유기성 폐기물 특성에 따라 복합 또는 개별장치로 용해성 콜로이드입자 전과 후처리로 오존산화 미세버블 및 전기분해 산화 응집부상 마이크로 버블처리로 난분해성 물질과 색도분해유도하는 단계(S60);가 포함됨을 특징으로 하는유기성 폐기물 및 폐액 균질화 고도전처리 방법.
Organic waste and waste liquid homogenization, which is an advanced pretreatment technology that can reduce the concentration of various pollutants, pathogens, viruses and odors, before being separated into organic waste and wastewater with high pollutant concentration of claim 1 Homogenization of organic waste and waste liquid using advanced pretreatment device It relates to an advanced pre-treatment method,
Separating only the hairs or foreign substances by using the screen 112 for removing the organic waste material to be treated, and supplying it to the water collecting tank 113 (S10);
In the step (S10), when the circulation stirring device 111 for preventing raw manure sedimentation blocks air through anaerobic circulation and suppresses the outflow of odor to the outside and transfers it to the screen 112 using a stirring pump, the screen 112 is used for livestock manure. In disposing of wastes to remove foreign substances from strictures, crushing, crushing, and removing strictures are processed livestock manure with a basic facility, and only hairs or foreign substances are separated and sent to the collection tank 113, thereby smoothing livestock manure. And transport it to the pump.
Thereafter, the step of inducing the separation of suspended substances through stabilization and solubilization of organic wastes using an activated radical pressure solubilization device 200 that decomposes and solubilizes organic matter in livestock manure (S20);
Subsequently, the solubilization-treated manure-free liquor (no agglomeration: no coagulant is not injected) is used to separate the sludge from the dewatering liquid using the dewatered sludge treatment device 300 (S30);
Thereafter, using the active decomposition circulator 400 including the ozone generator 411 to induce oxidative decomposition through a contact free radical reaction with the organic wastewater of the desorption liquid (S40);
Subsequently, using the decomposition flotation treatment device 500 to decompose and flotate the complex oxide material dissolved in the pressure decomposition flotation treatment (S50);
Afterwards, using the electrolysis oxidative coagulation flotation treatment device 600, depending on the characteristics of organic wastes, the ozone oxidation microbubbles and electrolysis oxidation coagulation flotation microbubbles are used to treat soluble colloid particles before and after treatment in a complex or separate device. The step of inducing chromaticity decomposition (S60); advanced pretreatment method for homogenizing organic waste and waste liquid, characterized in that it includes.
청구항 3 에 있어서,
상기 슬러지와 탈리액을 분리하는 단계(S30)는,
가축분뇨의 탈수슬러지와 탈리액을 분리하여 탈수슬러지는 퇴비화처리를 하도록 연계처리하며, 탈리액은 액비나 정화처리를 하도록 연계처리를 함을 특징으로 하는 유기성 폐기물 및 폐액 균질화 고도전처리 방법.
The method of claim 3,
The step of separating the sludge and the stripping liquid (S30),
An advanced pretreatment method for homogenizing organic waste and waste liquid, characterized in that the dewatered sludge of livestock manure is separated from the dewatering liquid, and the dewatered sludge is treated in conjunction with composting treatment, and the dewatering liquid is treated in conjunction with liquid manure or purification treatment.
청구항 3 에 있어서,
상기 탈리액의 유기성 폐수와 접촉 자유라디칼 반응으로 산화분해유도하는 단계(S40)는,
오존발생장치(411)와 활성라디칼산화장치(412)를 이용하여 활성라디칼을 1차, 2차 분해하여 탈리액의 유기성폐수와 접촉 자유라디칼 반응으로 산화분해유도함을 특징으로 하는 유기성 폐기물 및 폐액 균질화 고도전처리 방법.
The method of claim 3,
Inducing oxidation decomposition through a free radical reaction in contact with the organic wastewater of the desorption liquid (S40),
High level of homogenization of organic waste and waste liquid characterized by inducing oxidation and decomposition through a free radical reaction in contact with organic wastewater of the desorption liquid by primary and secondary decomposition of active radicals using the ozone generator 411 and the active radical oxidation device 412 Pre-treatment method.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115738161A (en) * 2022-11-14 2023-03-07 国网福建省电力有限公司 Method for degrading toxic and harmful substances in fire residues

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100478008B1 (en) 2003-07-25 2005-03-23 주식회사 무한기술 pre-treatment method and the device for livestock's sewage and excrements, sewage and sludge of sewage disposal tank
KR100903062B1 (en) 2008-08-29 2009-06-18 주식회사 부강테크 Processing unit for organic waste materials and method thereof
KR101051798B1 (en) * 2010-11-25 2011-07-25 (주) 엔티스 Waste water treatment apparatus using microbubbles
KR101092017B1 (en) 2008-12-08 2011-12-09 주식회사 이지바이오시스템 The Working Method of Continuous Thermophilic Anaerobic Co-Phase Digestion System using Waste Activated Sludge
KR101267054B1 (en) * 2013-04-10 2013-05-27 김완수 Method of recovery organic waste
KR101323277B1 (en) 2012-05-21 2013-10-29 (주)동화이앤씨 Wastewater treatment system and method thereof
KR102046833B1 (en) 2018-04-25 2019-11-21 (주)정수 Multipurpose Middle Water Purification Unit

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100478008B1 (en) 2003-07-25 2005-03-23 주식회사 무한기술 pre-treatment method and the device for livestock's sewage and excrements, sewage and sludge of sewage disposal tank
KR100903062B1 (en) 2008-08-29 2009-06-18 주식회사 부강테크 Processing unit for organic waste materials and method thereof
KR101092017B1 (en) 2008-12-08 2011-12-09 주식회사 이지바이오시스템 The Working Method of Continuous Thermophilic Anaerobic Co-Phase Digestion System using Waste Activated Sludge
KR101051798B1 (en) * 2010-11-25 2011-07-25 (주) 엔티스 Waste water treatment apparatus using microbubbles
KR101323277B1 (en) 2012-05-21 2013-10-29 (주)동화이앤씨 Wastewater treatment system and method thereof
KR101267054B1 (en) * 2013-04-10 2013-05-27 김완수 Method of recovery organic waste
KR102046833B1 (en) 2018-04-25 2019-11-21 (주)정수 Multipurpose Middle Water Purification Unit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115738161A (en) * 2022-11-14 2023-03-07 国网福建省电力有限公司 Method for degrading toxic and harmful substances in fire residues

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