KR20000072420A - Treatment method for livestock sewage and method of paddy rice fertilizer - Google Patents

Treatment method for livestock sewage and method of paddy rice fertilizer Download PDF

Info

Publication number
KR20000072420A
KR20000072420A KR1020000051894A KR20000051894A KR20000072420A KR 20000072420 A KR20000072420 A KR 20000072420A KR 1020000051894 A KR1020000051894 A KR 1020000051894A KR 20000051894 A KR20000051894 A KR 20000051894A KR 20000072420 A KR20000072420 A KR 20000072420A
Authority
KR
South Korea
Prior art keywords
solid
wastewater
liquid separation
waste water
livestock
Prior art date
Application number
KR1020000051894A
Other languages
Korean (ko)
Inventor
김재인
Original Assignee
김재인
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 김재인 filed Critical 김재인
Priority to KR1020000051894A priority Critical patent/KR20000072420A/en
Publication of KR20000072420A publication Critical patent/KR20000072420A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • 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
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/40Treatment of liquids or slurries
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D9/00Other inorganic fertilisers
    • C05D9/02Other inorganic fertilisers containing trace elements
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G1/00Mixtures of fertilisers belonging individually to different subclasses of C05
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

PURPOSE: Solid composting and fertilizer for water are provided to separate floating substances in highly concentrated livestock waste water without having inorganic phosphate or heavy metal by a solid-liquid separation method for producing high quality organic fertilizer. CONSTITUTION: A solid-liquid separation method of high concentration livestock waste water is performed by inputting sulfuric acid, hydrochloric acid and amino acid into the high concentration livestock waste water and by controlling pH 6.5-7. Active carbon powder or raw lime powder is input into the waste water and is adsorbed floating substances, nitrogen, phosphate or heavy metal. Oxidizing agents like PAC, aluminum oxide sulfate are input and aggregated by using a polymer aggregator after controlling pH 6.0-6.5. Floating substances are floated by using pressurizing floating tank. The solid-liquid separation method separates solid after passing through a screen. The solid-liquid separated colloidal solid is input to an aerobic fermenting system like ventilating fermenting tank, stirring-type fermenting tank or circular fermenting tank by mixing and stirring fly ash and waste wood for controlling brine rate, ventilation and coal quality rate proper to the aerobic fermentation.

Description

고농도 축산폐수의 고액분리와 고형물의 퇴비화 방법 및 수도용 비료{Treatment method for livestock sewage and method of paddy rice fertilizer}Treatment method for livestock sewage and method of paddy rice fertilizer}

국내 축산농가 567천호에서 배출하는 축산폐수는 1일간 약197천톤으로서 1년간 약70920천톤에 달한다.The domestic livestock wastewater discharged from domestic farmhouse 567 thousand lakes is about 197 thousand tons per day, which is about 7720 thousand tons per year.

오수분뇨 및 축산폐수의 처리에 관한 법율에 의거 축사를 설치하려는 자는 축사규모에 따라 시도지사의 축산분뇨 처리시설 설치허가를 받거나 시장군수에게 신고를 해야하며 방류수질 기준이하로 처리하는 시설을 설치하도록 하였다. 정부에서는 허가, 신고대상 이하의 소규모 축산농가에서 발생하는 폐수를 공동으로 수거하여 처리할 수 있도록 1991년 이후 국고지원사업으로 축산폐수공동처리시설을 설치하고 처리사업을 추진하여 1999년도 말 현재 전국에 12개소를 가동중에 있고, 29개소에 건설공사 및 시운전중에 있다. 현재 축산폐수공동처리장의 대부분이 폐수를 정화처리후에 방류하는 공법에 의한 시설설계기준이 BOD 5000mg/l인 처리시설에 유입폐수의 평균 BOD 는 20000∼30000mg/l의 고농도 폐수가 유입되어 처리가 원할이 되지않는 시스템의 문제점으로 지적되며 BOD,COD,질소, 인등 방류수질 기준에 적합한 처리가 곤란하고, 시설용량기준 50%이하의 폐수밖에 처리하지 못하는 문제점으로 지적되고 있다. 축산분뇨는 산업폐기물 배출량에 17%정도인데 고농도 폐수로서 생물학적산소요구량 (BOD)의 총부하량은 각종 산업폐수의 47%로 가장 높다. 이들 축산폐수를 적정 처리하지 않고 방류시에 하천의 수질악화와 지하수오염, 호소의 부영양화를 초래하여 상수원과 농업용수를 오염시킬 뿐아니라 악취 침출수 해충피해등 쾌적한 생활환경을 파괴하는 요인이 되고있다, 기존의 고농도 축산폐수의 처리방법에는 활성오니방법, 저장액비화방법 살수여상방법, 퇴비화방법등 여러가지 방법이 있으나 다량 배출되는 축산폐수의 효율적인 고액분리를 위한 방법은 단순히 중화처리하여 고형물을 응집하는 방법으로 부유고형물의 분리 효율이 30∼40%를 넘지 못하였다.According to the law on the treatment of sewage manure and livestock waste water, a person who intends to install a livestock house must obtain permission to install livestock manure treatment facilities of the municipal government or report to the mayor of the mayor according to the scale of the livestock, and install a facility that treats discharged water quality standards or less. It was. Since 1991, the government has established a joint livestock wastewater treatment facility as a national government support project and promoted the treatment project to jointly collect and treat wastewater generated from small-scale livestock farms under license and report. Twelve locations are in operation, and 29 are under construction and commissioning. Currently, most of the livestock wastewater treatment plants have a BOD 5000mg / l facility design standard by the method of discharging the wastewater after purification, and the average BOD of the influent wastewater is 20000 ~ 30000mg / l. This problem is pointed out as a problem of the system, and it is pointed out that it is difficult to treat the discharge water quality standards such as BOD, COD, nitrogen, and phosphorus, and only waste water of 50% or less of facility capacity is treated. Livestock manure is about 17% of industrial waste emissions, and the high concentration of biological oxygen demand (BOD) is 47% of all industrial wastewater. When discharging these livestock wastes without proper treatment, it causes water quality deterioration, groundwater pollution and eutrophication of lakes, and contaminates water supply and agricultural water as well as destroys pleasant living environment such as odorous leachate pest damage. Conventional methods for treating high concentration livestock wastewater include active sludge method, storage liquid fertilization method, sprinkling water filter method, and composting method.However, the method for efficient solid-liquid separation of large-scale livestock wastewater is simply neutralized to agglomerate solids. The separation efficiency of suspended solids did not exceed 30-40%.

따라서 국내외 적으로 고농도 축산폐수의 처리방법에 많은 연구와 기술개발에 투자를 하고 있지만 기술에 한계가 있어 축산폐수공동처리 정책적인 재검토와 가축사육을 제한하거나 폐수방류수질 기준을 강화하고있어 축산폐수 처리기술 개발은 환경보전 측면 뿐아니라 축산업의 안정적인 발전을 위한 가장 큰 문제점으로 지적되고 있다.As a result, we invest a lot of research and technology development in the treatment method of high concentration livestock wastewater at home and abroad, but there are limitations in technology, so we have to revise the policy on livestock wastewater treatment and restrict the livestock raising or strengthen the wastewater discharge water quality standard. Technology development has been pointed out as the biggest problem for stable development of livestock industry as well as environmental conservation.

축산폐수는 생활오수나 공장폐수와는 달리 고농도 유기성분으로서 무기인이나 중금속이 함유되지 않았고 미생물의 발효분해가 용이하여 양질의 유기질비료로 자원화가 가능하다. 따라서 축산폐수공동처리장에 유입되는 BOD 20000∼30000mg/l의 고농도 축산폐수를 무리하게 정화처리후 방류하는 방법을 지양하고, 기 설치된 축산폐수정화처리시설의 유입폐수 처리사설기준 BOD 5000mg/l에 적합한 수질기준으로 고농도 축산폐수에 함유된 부유물질을 분리하는 고액분리기술을 제공하는데 있다.Unlike domestic wastewater and factory wastewater, livestock wastewater does not contain inorganic phosphorus or heavy metals as a high concentration of organic components, and it is easy to ferment and decompose microorganisms, so it is possible to resource it with high quality organic fertilizer. Therefore, avoid the method of purifying and discharging BOD 20000 ~ 30000mg / l high concentration livestock wastewater flowing into the livestock wastewater treatment plant forcibly and complying with BOD 5000mg / l. It is to provide a solid-liquid separation technology for separating suspended solids contained in high concentration livestock wastewater on the basis of water quality.

고농도 축산폐수에 함유한 부유물질을 적은 약품처리로 70∼80%의 고형물과 질소 인을 분리해서 전체 폐수중량비 15∼20%의 콜로이드상 물질로 응집 배출되는 고형물을 호기성발효방법으로 퇴비화 재활용하여 폐수처리비용을 절감하고 저농도폐수로 고형물을 제거한 축산폐수의 처리용량을 극대화하며, 방류수질을 규제이하로 효율적인 처리방법을 도모하는 환경친화적인 고농도축산폐수의 고액분리와 고형물의 퇴비화 방법을 제공하는데 있다.Treating suspended solids in high concentration livestock wastes with low chemical treatment, separating 70-80% of solids and nitrogen phosphorus and composting and discharging solids with 15 to 20% of colloidal material by weight of total wastewater by composting and recycling wastewater To reduce treatment costs, maximize the treatment capacity of livestock wastewater from which solids are removed with low concentration wastewater, and provide a method for solid-liquid separation and solid composting of environmentally-friendly high concentration livestock wastewater to promote efficient treatment methods under the regulation of discharged water quality. .

본 발명은 함수율 70∼80%의 콜로이드상 물질을 호기성발효에 적합한 초기함수율 60∼65%로 함수율, 통기성, 탄질율 (C/N)을 조절하기 위하여 플라이 애쉬 (fly ash)와 폐목재를 분쇄한 목분, 수피분, 우드칩 (wood chip) 특별히 제조한 수분조절재 (특허등록제 0220210호) 를 혼합 교반하여 통풍식 발효조, 교반식 발효조, 기타 호기성 발효시스템에 투입하고 공기를 주입하면서 70∼85℃의 고온으로 발효시켜 단시간내에 퇴비를 제조하고 여기에 논토양 개량에 필요한 영양분을 첨가하여 수도용비료로 토양에 환원하므로서 목적을 달성하였다.In the present invention, the fly ash and waste wood are pulverized to adjust the water content, breathability, and carbon content (C / N) at an initial water content of 60 to 65% suitable for aerobic fermentation of the colloidal material having a water content of 70 to 80%. Wood flour, bark meal, wood chip (Moisture regulating agent No. 0220210) specially prepared by mixing and stirring, into the ventilation fermentation tank, stirred fermentation tank, other aerobic fermentation system and injecting air 70 ~ 85 The fermentation was carried out at a high temperature of ℃ to produce a compost within a short time and by adding the nutrients necessary for paddy soil improvement to reduce to the soil as a water fertilizer to achieve the object.

이하 본 발며의 구성을 설명한다.The configuration of the present invention will be described below.

도 1 은 고농도 추산폐수의 고액분리 공정도1 is a flow diagram of solid-liquid separation of high-estimate wastewater

도 2 는 고형물의 퇴비화 공정도2 is a composting process diagram of the solids

본 발명은 고농도축산폐수의 부유물질과 질소, 인을 분리하여내는 공정과 분리한 콜로이드상 고형물질을 퇴비화하는 공정과 고액분리폐수를 기존의 축산폐수정화장에 투입하여 정화처리 방류하는 공정으로 구성되며 본 발명은 고액분리공정과 고형물의 퇴비화공정으로 구성된다.The present invention consists of a process for separating suspended solids, nitrogen and phosphorus from high concentration livestock wastewater, a process for composting separated colloidal solid matter, and a process for purifying and discharging the solid-liquid separation wastewater into an existing livestock wastewater purification plant. The present invention consists of a solid-liquid separation process and a composting process of solids.

축산폐수공동처리장의 시설용량에 따라 매일매일 처리하는 폐수량을 저장이 가능한 저장조 2개를 설치하여 1차 저장조의 폐수를 다음 날에 고액분리 처리공정 ; 축산폐수에 산, 아미노산액을 이용하여 pH를 약산성 범위인 7∼6, 5까지 저하시켜 폐수에 함유된 부유물질, 질소, 인등의 산화촉매 반응을 일으키고, 활성탄분말이나 생석회분말을 이용하여 부유물질을 흡착시킨 뒤 ; PAC나 황산반토와 같은 산화제를 넣으면서 pH를 6, 0∼6, 5까지 조절한다 ; 고분자응집제를 이용하여 응집시킨후 가압부상조를 이용하여 부유물질을 부상시켜 스크린을 통과 고형물을 순간적으로 분리해내는 운전이 단순하며 고액분리 효율이 높은 화학처리방법 ; 고농도축산폐수에 함유한 부유물질의 약 80%를 폐수중량 10∼20%로 응집하여 분리하여낸 콜로이드상 고형물을 초기함수율 60∼65%로 수분조절하고 통기성, 탄질율 (C/N)을 조절하기 위하여 Fly ash 와 폐목재를 분쇄한 목분, 수피분, Wood chip 이나 특별히 제조한 수분조절재 (특허등록 제0220210호) 를 혼합 교반 ; 통풍식발효조, 교반식발효조, 기타 호기성 발효시스템에 투입하고 70∼85℃의 고온으로 발효를 진행시키므로 유해성 병원균이나 기생충란, 잡초씨가 사멸되며 유해성 유기물이 호기성미생물에 의하여 산화와 합성 등 생화학적 반응을 통하여 년평균 10∼15일간에 속성으로 퇴비화 한다 ; 호기성 발효 퇴비에 논토양 개량제와 영양소를 첨가하여 수도용비료를 제조한다 ;Solid-liquid separation process of the wastewater from the primary storage tank by installing two reservoirs that can store the amount of wastewater treated every day according to the facility capacity of the livestock wastewater treatment plant; Acid and amino acid liquids are used in livestock wastewater to reduce the pH to 7 ~ 6 and 5, which are weakly acidic, causing oxidation catalyst reactions of suspended solids, nitrogen, and phosphorus in the wastewater, and suspended solids using activated carbon powder or quicklime powder. After adsorbing; Adjust the pH to 6, 0 to 6, 5 while adding an oxidizing agent such as PAC or alumina sulfate; A method of chemically treating solids with high efficiency and solid-liquid separation efficiency by flocculating with a polymer flocculant and then using a floating flotation flotation to float suspended matter and passing solids through the screen. About 80% of the suspended solids contained in the high concentration livestock wastewater are separated by coagulation of 10 ~ 20% by weight of wastewater, and the water content is controlled by the initial water content of 60 ~ 65%, and the air permeability and carbon mass rate (C / N) are controlled. Mixing and stirring fly ash, waste wood, bark flour, wood chips or specially prepared moisture control material (Patent No. 0220210) for the purpose of grinding; It enters into a ventilated fermentation tank, a stirred fermentation tank, and other aerobic fermentation systems, and fermentation proceeds at a high temperature of 70-85 ° C. Therefore, harmful pathogens, parasites, and weed seeds are killed. Compost through the property in an average of 10 to 15 days per year; Water fertilizer is prepared by adding paddy soil improver and nutrient to aerobic fermentation compost;

이하, 본 발명에 구체적인 방법을 실시예를 들어 상세히 설명한다.Hereinafter, the present invention will be described in detail by way of examples.

실시예 1 ; 고농도 축산폐수의 고액분리와 고형물의 퇴비화Example 1; Solid-liquid Separation of High-Livestock Wastewater and Composting of Solids

제 1 공정 ; 산화촉매반응단계First process; Oxidation catalyst reaction step

축산폐수저장조의 폐수량 200ml에 황산, 염산 아미노산등 산화제를 1, 0∼1, 5ml를 투여하여 pH를 6, 5∼7, 0로 조절한다.The pH is adjusted to 6, 5-7, 0 by administering 1, 0-1, 5ml of oxidizing agents such as sulfuric acid and hydrochloric acid to 200ml of wastewater storage tank.

축산폐수저장조에 직접 산화제를 투여하면 거품이 급격하게 발생하게 되는데 이는 산화제가 축산폐수의 유기물과 더불어 이온화 결합이 일어나고 이대 결합된 슬러지가 비중차에 의해 위로 부상하기 때문이다.When the oxidant is directly injected into the livestock wastewater storage tank, bubbles are generated rapidly because the oxidant is ionized with the organic matter of the livestock wastewater and the combined sludge rises due to the specific gravity difference.

따라서 이러한 거품으로 인해 흡착화학공정을 효율적으로 운전하기가 어려워진다. 이러한 단점을 극복하기 위해서는 먼저 전처리공정을 거쳐서 산화제를 서서히 투입하여 약산성에 이르도록 하였다Therefore, these bubbles make it difficult to operate the adsorption chemical process efficiently. In order to overcome these disadvantages, the oxidant is gradually added to the weak acid through the pretreatment process.

제 2 공정 ; 흡착공정단계Second process; Adsorption Process Step

산화촉매반응단계를 거친 축산폐수에 활성탄분말이나 생석회분말을 이용하여 미세한 부유물질, 질소, 인, 색도를 이르키는 물질을 흡착하는 공정이다. 이 반응의 균일화를 위해 교반기를 설치하고, 산화제인 PAC, 황산반토 등을 이용하여 pH를 6, 0∼6, 5%까지 조정하였다.It is a process of adsorbing fine suspended solids, nitrogen, phosphorous, and chromatic substances by using activated carbon powder or quicklime powder in livestock wastewater which has undergone oxidation catalyst reaction step. In order to homogenize this reaction, the stirrer was installed and pH was adjusted to 6, 0-6, 5% using PAC, alumina sulfate, etc. which are oxidizing agents.

제 3 공정 ; 가압부상응집공정Third process; Pressurized Flotation Flocculation Process

흡착반응이 진행된 후에 곧바로 고분자 응집제를 이용하여 부유물질을 부상시켜 응집시킨후 가압부상조와 스크린을 통과 고형물질을 순간적으로 분리해내는 운전이 단순하며 분리효율이 높은 화학처리 방법이 된다.Immediately after the adsorption reaction is carried out, the flocculant is floated using the polymer flocculant to flocculate the flocculant, and then the operation of separating the solid matter momentarily through the pressure relief tank and the screen is a simple and highly efficient chemical treatment method.

제 4 공정 ; 수분조절재 혼합교반Fourth process; Mixing of moisture control material

고액분리한 함수율 70∼80%의 콜로이드상 고형물에 호기성 발효에 적합한 함수율, 통기성, 탄질율을 조절하기위하여 Fly ash 70∼90중량%와 폐목재를 분쇄한 목분 10∼30중량%를 혼합교반하여 발효시스템에 투입하였다.70-90% by weight of fly ash and 10-30% by weight of pulverized wood powder were mixed and mixed in order to control the water content, breathability, and carbon content suitable for aerobic fermentation in the colloidal solids having a water content of 70-80% of solid-liquid separation. It was put into the fermentation system.

제 5 공정 ; 발효공정Fifth process; Fermentation Process

발효시스템은 퇴비제조용량에 따라 피트길이 60∼100m, 넓이 4∼8m 깊이 1, 5∼2, 0m 크기의 터널식 발효조, 피트직경 10∼25m, 깊이 2, 0∼2, 5m 의 원형발효시스템, 피트높이 2, 0m, 폭2, 5∼3m , 길이 5∼6m 통풍식 발효시스템을 이용하여 1일 20∼30㎥ 의 혼합물질을 투입하고 발효조의 바닥에 공기를 강제로 주입할 수 있는 파이프라인에 연결한 발효조 측면부에 설치된 강력한 송풍기를 이용하여 발효건조에 필요한 공기를 24시간 간단없이 공급하였다. 동절기에는 호기성미생물의 활성화를 돕기 위하여 열파이프로 열을 공급하여 발효기간중 70∼85℃의 고온으로 5∼7일간 지속되며 10∼15일이후에는 함수율 40%, 발효조 내부온도 30∼40℃가 되어 발효가 완성 되었다.The fermentation system is a tunnel fermenter with a pit length of 60 to 100m, a width of 4 to 8m and a depth of 1, 5 to 2, 0m, a round fermentation system of 10 to 25m in pit diameter and a depth of 2, 0 to 2, 5m depending on the compost production capacity. Pipeline that can inject 20 ~ 30㎥ of mixture material per day and force air into the bottom of fermenter by using ventilated fermentation system with pit height 2, 0m, width 2, 5 ~ 3m, length 5 ~ 6m Using a powerful blower installed in the fermenter side connected to the air supply for the fermentation drying simply 24 hours. In winter, heat is supplied by heat pipe to help activate aerobic microorganisms, and it lasts 5-7 days at high temperature of 70-85 ℃ during fermentation period.After 10-15 days, water content 40% and internal temperature of fermentation tank are 30-40 ℃. Fermentation was completed.

제 6 공정 ; 수도용비료 제조6th process; Water Fertilizer Manufacturing

상기 제 5 공정에서 제조하에 원형스크린으로 정선하여 미발효 목편은 초기 혼합교반조로 리사이크링하며, 완숙 퇴비 60∼70중량%에 논토양 개량제로 Fly ash 10∼20중량%와 영양소로 아미노산 10∼20중량%를 혼합하여 20kg단위로 PE포대에 포장하여 수도용비료를 제조한다.The fermented wood pieces are selected by a circular screen under the manufacturing process in the fifth step, and recycled with an initial mixing agitator. The fermentation compost is 60 to 70% by weight, 10 to 20% by weight of fly ash as a soil improvement agent and 10 to amino acids as nutrients. 20% by weight of 20% by weight in a PE bag to prepare a fertilizer for water.

고농도축산폐수 500ml에 황산을 투입하여 pH를 6, 5∼7, 0, 약산성으로 조정하고 PAC나 황산반토를 3ml투입하여 pH를 6, 0∼6, 5로 조정하여 처리하여 BOD, TN (총질소) TP (총인)이 80%이상 제거되며 활성탄분말로 전처리 할 경우 BOD, TN, TP이 85∼90%의 회수되어 콜로이드상 고형물로 퇴비화에 재활용 되고, 고액분리로 전처리된 저농도폐수의 정화처리효율이 높아지는 환경친화적인 유용한 발명이다Sulfuric acid was added to 500ml of high concentration livestock wastewater to adjust pH to 6, 5 ~ 7, 0, slightly acidic, and 3ml of PAC or alumina sulfate was adjusted to pH 6, 0 ~ 6, 5 to treat BOD, TN (total Nitrogen) TP (total phosphorus) is removed more than 80%, and pretreatment with activated carbon powder recovers 85 ~ 90% of BOD, TN, TP and recycles it for composting into colloidal solids, and purifies low concentration wastewater pretreated by solid-liquid separation. It is an eco-friendly and useful invention that increases efficiency.

본 발명 방법으로 제조한 수도용비료에는 논토양에 부족한 토양미생물과 유기물, 규산, 석회, 고토, 미량원소 등 토량개량제를 고르게 함유한 수도용 복합토양개량제가 되며 논토양에 객토, 퇴비, 규산질비료, 미량원소와 비료삼요소 (질소, 인산, 가리) 를 동시에 시용하는 효과가 있는 노동력 절감형 복합비료를 제조하는 기술과 그 비료를 특징으로 한다.The water fertilizer prepared by the method of the present invention is a complex soil improver for water, which contains soil microorganisms, organic matter, silicic acid, lime, koto, and trace elements, which are insufficient in paddy soil, and has soil, compost, siliceous fertilizer, trace amount in paddy soil. It is characterized by the technology of manufacturing labor-saving compound fertilizers with the effect of simultaneously applying elemental and fertilizer trielements (nitrogen, phosphoric acid, and garlic) and its fertilizers.

시험기관 ; 농업과학기술원, 한국생활용품연구원.Test institute; Institute of Agricultural Science and Technology, Korea Household Goods Research Institute.

Claims (2)

고농도 축산폐수에 황산, 염산, 아미노산을 투여하여 pH 6, 5∼7, 0로 조절하고 활성탄분말이나 생석회분말을 폐수에 투입하여 부유물질이나, 질소, 인, 중금속을 흡착시키고, PAC, 황산반토 등 산화제를 투입하여 pH를 6, 0∼6, 5로 조절한 후에 고분자응집제를 이용하여 응집시킨후 가압부상조를 이용하여 부유물질을 부상시키고 스크린을 통과하여 고형물을 분리하는 고농도축산폐수의 고액분리 방법.Sulfuric acid, hydrochloric acid and amino acid are administered to high concentration livestock wastewater to adjust pH to 6, 5 ~ 7, 0. Activated carbon powder or quicklime powder is added to the wastewater to adsorb suspended solids, nitrogen, phosphorus and heavy metals. After adjusting the pH to 6, 0 ~ 6, 5 by adding oxidizing agent, agglomerate using polymer coagulant, and then using floating flotation tank to float the suspended solids and go through the screen to separate solids. Separation method. 고액분리한 콜로이드상 고형물을 호기성 발효에 적합한 함수율, 통기성, 탄질율을 조절하기 위하여 Fly ash 와 폐목재를 분쇄한 목분 등 수분조절를 혼합교반하여 통풍식 발효조, 교반식 발효조, 원형식 발효조 등 호기성 발효시스템에 투입하여 70∼85℃의 호기성 고온발효로 10∼15일간의 속성발효한 퇴비에 논토양에 필요한 영양분을 첨가하여 제조한 수도용 복합토양개량제 그 제조방법.Aerobic fermentation such as ventilated fermenter, stirred fermenter, round fermenter, etc. A method for producing a complex soil improver for water, prepared by adding nutrients necessary for paddy soil to compost fermented for 10 to 15 days by aerobic high temperature fermentation at 70 to 85 ° C. in a system.
KR1020000051894A 2000-09-02 2000-09-02 Treatment method for livestock sewage and method of paddy rice fertilizer KR20000072420A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020000051894A KR20000072420A (en) 2000-09-02 2000-09-02 Treatment method for livestock sewage and method of paddy rice fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020000051894A KR20000072420A (en) 2000-09-02 2000-09-02 Treatment method for livestock sewage and method of paddy rice fertilizer

Publications (1)

Publication Number Publication Date
KR20000072420A true KR20000072420A (en) 2000-12-05

Family

ID=19687032

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020000051894A KR20000072420A (en) 2000-09-02 2000-09-02 Treatment method for livestock sewage and method of paddy rice fertilizer

Country Status (1)

Country Link
KR (1) KR20000072420A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100856063B1 (en) 2007-06-22 2008-09-02 조재영 Method for preparation of organic substrate by removing heavy metals and sterilizing pathogenic microorganisms through electric beam and exposing gamma;-ray from livestock
CN111349441A (en) * 2020-04-10 2020-06-30 绍兴市农业科学研究院 Method for safely utilizing As and Pb composite pollution of farmland soil

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR830000183A (en) * 1978-12-19 1983-03-30 도오루 세끼 How to treat sewage sludge and manure by pulverized coal
JPH0782069A (en) * 1993-09-09 1995-03-28 Shin Nippon Rakunou Kenkyusho:Kk Compost preparation process
JPH07275900A (en) * 1994-04-07 1995-10-24 Yoshio Gomi Method for treating wastewater containing organic substance
JPH11228267A (en) * 1998-02-17 1999-08-24 Nippon Paper Industries Co Ltd Production of fertilizer from organic sludge
KR100220210B1 (en) * 1997-04-04 1999-09-01 김재인 Method for producing fertilizer
KR100285298B1 (en) * 1999-05-29 2001-03-15 최주식 A disposal method of pig ordure

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR830000183A (en) * 1978-12-19 1983-03-30 도오루 세끼 How to treat sewage sludge and manure by pulverized coal
JPH0782069A (en) * 1993-09-09 1995-03-28 Shin Nippon Rakunou Kenkyusho:Kk Compost preparation process
JPH07275900A (en) * 1994-04-07 1995-10-24 Yoshio Gomi Method for treating wastewater containing organic substance
KR100220210B1 (en) * 1997-04-04 1999-09-01 김재인 Method for producing fertilizer
JPH11228267A (en) * 1998-02-17 1999-08-24 Nippon Paper Industries Co Ltd Production of fertilizer from organic sludge
KR100285298B1 (en) * 1999-05-29 2001-03-15 최주식 A disposal method of pig ordure

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100856063B1 (en) 2007-06-22 2008-09-02 조재영 Method for preparation of organic substrate by removing heavy metals and sterilizing pathogenic microorganisms through electric beam and exposing gamma;-ray from livestock
CN111349441A (en) * 2020-04-10 2020-06-30 绍兴市农业科学研究院 Method for safely utilizing As and Pb composite pollution of farmland soil

Similar Documents

Publication Publication Date Title
CN107010788B (en) Large-scale pig farm cultivation wastewater treatment system and method
CN103922538B (en) Livestock and poultry breeding wastewater treatment method
CN104211168B (en) The method for carrying out anaerobic digestion to waste water in upflow type anaerobic digester and Sludge Bed using zeolite-clinoptilolite
CN102408177A (en) Biological complex enzyme for sludge recycling and use method thereof
WO2014094484A1 (en) Garbage leachate treatment method and system
WO2010003255A1 (en) Process for continual multiphase recycling of solid and liquid organic waste for a greenhouse culture
CN110304736A (en) A kind of slow-release complex microorganism growth-promoting agent and preparation method and purposes
CN101700951A (en) Emulsified liquid waste water treatment method
Zheng et al. Pilot-scale experiments on multilevel contact oxidation treatment of poultry farm wastewater using saran lock carriers under different operation model
LaPara et al. Autothermal thermophilic aerobic waste treatment systems: A state-of-the-art review
Guo et al. Optimization of high-rate TN removal in a novel constructed wetland integrated with microelectrolysis system treating high-strength digestate supernatant
Deng et al. Treatment and utilization of swine wastewater–A review on technologies in full-scale application
CN209740874U (en) Biogas slurry treatment device
CN105152480A (en) Municipal sewage treatment method
CN105271618B (en) Reinforced sewage processing system and method
CN113698049A (en) Process for treating and recycling pig-raising wastewater containing water-washed manure and water-soaked manure
CN113072260A (en) Treatment method of enhanced nitrogen and phosphorus removal resource recycling pig raising wastewater
EP2279153B1 (en) Method for treating and/or pretreating liquid manure or biogas plant reject for the elimination of harmful substances, particularly nitrogen, phosphorus, and odor molecules
KR20130123799A (en) Method for treating organic waste matter
CN107399891B (en) Livestock and poultry manure recycling process and method
CN215288415U (en) Autotrophic nitrogen removal system for pure membrane MBBR (moving bed biofilm reactor) coupled carbon capture
CN212425605U (en) Deodorant sewage treatment system
KR20000072420A (en) Treatment method for livestock sewage and method of paddy rice fertilizer
KR970002486B1 (en) Apparatus and method for waste water treatment
CN204369720U (en) Culturing wastewater processing system

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E601 Decision to refuse application