KR20100049229A - Disposal method of an organism waste mulitiprosess digests - Google Patents

Disposal method of an organism waste mulitiprosess digests Download PDF

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KR20100049229A
KR20100049229A KR20080108313A KR20080108313A KR20100049229A KR 20100049229 A KR20100049229 A KR 20100049229A KR 20080108313 A KR20080108313 A KR 20080108313A KR 20080108313 A KR20080108313 A KR 20080108313A KR 20100049229 A KR20100049229 A KR 20100049229A
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organic
organic material
biogas
tank
waste
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KR20080108313A
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Korean (ko)
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장승권
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(주)바이오텍스
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2813Anaerobic digestion processes using anaerobic contact processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • C02F11/04Anaerobic treatment; Production of methane by such processes
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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
    • Y02W30/20Waste processing or separation

Abstract

PURPOSE: A multi-digesting treatment method of organic waste in an independent facility is provided to activate digestion action of microorganism when the organic waste is stored in a multi-digesting treatment system, and to uniformly maintain concentration of organic materials. CONSTITUTION: A multi-digesting treatment method of organic waste in an independent facility includes a step for crushing and storing the organic waste, a step for digesting the organic waste, a step for discharging gas, and a step for discharging liquid fertilizer in one process. A raw material is agitated in a first agitating and foreign material removing tank(40). A partition(31,32,33,34) installed on each digestion tank makes an inner wall and a flow path to digest the organic materials.

Description

독립시설물의 유기성폐기물 다중소화처리방법 {DISPOSAL METHOD OF AN ORGANISM WASTE MULITIPROSESS DIGESTS}  Organic waste multi-digestion treatment of independent facilities {DISPOSAL METHOD OF AN ORGANISM WASTE MULITIPROSESS DIGESTS}

본 발명은 독립시설물의 유기성폐기물 다중소화처리방법, 보다 상세하게는 축산 분료 등 처리하는 외국의 기술 등은 원형의 일반 탱크에 유기성폐기믈을 저장하여 발효시키는 방법을 사용하고 있는데 이는 동력이 끈기는 경우 막대한 비용으로 만들어진 플랜트가 그 기능을 사용할 수 없는 상황이 벌어지며, 하나의 공간에서 발효하기 때문에 소화균등의 비율이 깨저 소화능력이 저하되면, 수천톤의 유기물질을 다시 소화조에서 꺼내야 하는 일이 벌어진다.  The present invention is a method of multi-digestion treatment of organic waste of independent facilities, more specifically, foreign technology such as livestock powder is used to ferment by storing organic waste in a circular general tank, which is difficult to power If a plant made at a huge cost cannot use its function, and fermentation in one space leads to a breakdown in digestibility, it is necessary to remove thousands of tons of organic material from the digester. It happens

또한 하수처리 시설이 마련되지 않은 도서, 산간, 오지 지역에서 생활할 때 발생되는 인체의 배설물 및 축분, 음식물쓰레기 등을 환경에 친화적인 상태로 처리함과 아울러 연료 또는 비료로 활용할 수 있게 한 독립시설물의 유기성폐기물 다중소화처리방법에 관한 것이다.In addition, it is an independent facility that can be used as fuel or fertilizer as well as treating environmental excrement, animal waste, and food waste generated when living in islands, mountains, and remote areas where sewage treatment facilities are not provided. The present invention relates to a method for treating multiple wastes of organic waste.

2012년유기물해양투기금지의 런던협약 및 고 유가시대에 페기물의 친환경처리 및 대체재생에너지를 생산하여 고유가의 수입대체 효과를 함께 해결하고, 일반적으로, 밀집된 주거지역에서는 주거환경과 공공위생을 고려하여 일상 생활에서 필수적으로 파생되는 생활폐기물을 위한 제반 시설이 이미 마련되어 있으나, 밀집 주거지역으 로부터 떨어진 농, 어촌 지역에서는 위생관련 시설을 자체적으로 해결하였다.In 2012, the London Convention on the Prohibition of Organic Maritime Affairs and the High Oil Price era solved the import substitution effect of high oil prices by producing eco-friendly treatment and alternative renewable energy.In general, in dense residential areas, considering residential environment and public hygiene, There are already facilities for domestic waste that are essential to daily living, but sanitation-related facilities have been resolved in farming and fishing villages away from dense residential areas.

즉, 급수와 하수시설을 독자적으로 구축하여 생활 오폐수를 처리하였으므로 시설비용이 매우 과중한 반면, 오염물의 처리 효율이 떨어지게 되었음은 물론 미처리된 하수를 자연에 방출시킴으로써 2차 오염을 유발하는 결점이 있었다.In other words, since the sewage and sewage facilities were built independently to treat domestic wastewater, the cost of the facility was very heavy, while the treatment efficiency of pollutants was reduced, and there was a drawback of causing secondary pollution by releasing untreated sewage into nature.

특히, 땜이나 취수원에 인접된 지역 또는 급수와 하수설비가 불가능한 지역에서는 대부분이 재래식에 의존하여 유기성폐기물을 처리함으로써 비위생적이고 처리방법이 불편하였음은 물론 심한 경우에는 수질을 오염시키게 되는 문제점이 있었다.In particular, in the area adjacent to the soldering or intake source or in the area where the water supply and sewage facilities are impossible, most of them rely on conventional methods to treat organic waste, which is unsanitary and inconvenient for treatment, and contaminates water quality in severe cases.

유기성폐기물처리방법으로 유기물질을 저장탱크에 잔류되게 한 상태에서 혐기성균의 활동에 의해 미생물이 소화작용을 일으키면서 오니를 발효 및 안정화시켜 메탄가스를 생산하게 된 기술이 공지되었다.It is known that the organic waste treatment method produces a methane gas by fermenting and stabilizing sludge as microorganisms are digested by the activity of anaerobic bacteria in a state in which organic substances remain in a storage tank.

그러나 상기 종래의 발효식 처리방법은 전기 등 동력원이 없는경우 탱크내에 저장된 유기물질이 시간의 경과에 의해 슬러지 형태로 딱딱하게 응고 및 침전되므로 함수율이 높은 유기물질이 저장탱크에 투입될 때 교반이 제대로 이루어지지 않게 되었고, 이에 의해 농도가 변화되면서 미생물의 소화기능에 장애가 유발되는 문제점이 있었다.However, in the conventional fermentation treatment method, when there is no power source such as electricity, the organic material stored in the tank solidifies and precipitates in the form of sludge over time, so that the agitation is properly performed when the organic material having high moisture content is introduced into the storage tank. It was not made, thereby changing the concentration there was a problem that causes disorders in the digestive function of microorganisms.

또한 상기와 같이 농도의 변화로 인하여 저장된 유기물질의 소화기능이 상실될 경우 저장기능도 상실되면서 포화상태가 초래되어 새로운 처리시설을 마련해야 되는 결점도 있었다 .In addition, if the extinguishing function of the stored organic material is lost due to the change in concentration as described above, there is also a drawback that the storage function is also lost, resulting in a saturation state and a new treatment facility must be prepared.

본 발명은 위와 같은 종래의 문제점을 감안하여 안출한 것으로서, 그 목적은 유기성폐기물을 다중소화시스템에 저장하여 처리할 때 미생물의 소화활동을 활성화시킬 수 있는 독립시설물의 유기성폐기물 다중소화처리방법을 제공하는 것이다.  The present invention has been made in view of the above-mentioned conventional problems, and an object thereof is to provide an organic waste multiple digestion treatment method of an independent facility that can activate the digestion activity of microorganisms when the organic waste is stored and treated in a multiple digestion system. It is.

본 발명의 다른 목적은 동력원이 제공되거나 또는 제공되지 않을 시에도 안정적으로 시스템내에 저장된 유기물질의 의 응고 및 침전으로 인한 슬러지화를 방지하여 항상 균일한 농도를 유지할 수 있는 독립시설물의 유기성폐기물 처리방법을 제공함에 있다.Another object of the present invention is an organic waste treatment method of an independent facility that can maintain a uniform concentration at all times, even when a power source is provided or not, stably prevents sludge formation due to solidification and precipitation of organic substances stored in the system. In providing.

이러한 목적을 달성하기 위한 본 고안은, 유기성폐기물이 저장되는 탱크를 그 투입구로부터 유기물을 발효시켜 바이오가스를 생성하게 구성하되 저장탱크의 내부에 모터의 구동에 의해 간헐적으로 교반되면서 응고 또는 침전현상을 방지하는 교반장  The present invention for achieving the above object, the organic waste is stored in the tank in which the organic waste from the inlet is configured to produce biogas, while the intermittent stirring by the operation of the motor inside the storage tank to solidify or settle phenomenon Stirring cabinet to prevent

치를 설치하며, 상기 탱크의 내부에 미생물의 활성에 적합한 적정온도를 유지하는 열병합발전장치와 pH 조정장치, 황산가스를 제거하는 탈황장치, 바이오가스 중의 수분 및 실록산을 제거가는 장치 등 설치함에 따라, 고분자의 유기성물질을 효율적으로 처리하고 재생에너지 즉 전기, 온수, 바이오가스, 퇴비 등 100%의 유기성폐기믈을 0%의 폐기성 잔재물을 남기지 않는 소화시스템을 특징으로한다.And a cogeneration system for maintaining a suitable temperature suitable for microbial activity, a pH adjusting device, a desulfurization device for removing sulfuric acid gas, a device for removing water and siloxane in biogas, etc. It efficiently handles organic materials of polymers and features a fire extinguishing system that does not leave 0% of waste residues and 100% of organic wastes such as renewable energy, electricity, hot water, biogas, and compost.

또한 총7회에 거처 소화처리하는 시스템으로 일부 초식동물의 4개의 위장을 가지고 단계별로 소화하여 먹이가 가지고있는 에너지원을 최대한 체내 흡수하고 바깥으로 버리는 소화시스템을 응용하여, 고안되었으면 총 7회에 거쳐 단계별로 각각의 독립적으로 소화처리하여 최종 알카리성 액비로 분해되어 퇴비화까지 되어 배출하는 것이 특징이다In addition, it is digested and processed in seven times. It is digested in stages with four gastrointestinals of some herbivores, and it applies the digestive system that absorbs the energy source of food as much as possible and discards it outward. It is characterized by discharging each individual step by step and dissolving it into final alkaline liquid fertilizer until it is composted and discharged.

이와 같은 본 발명의 독립시설물의 유기성폐기물 다중소화처리방법은 사람이 생활하는 과정에 필수적으로 발생되는 유기성폐기물과 축산분료 본시설물을 이용하여 보다 친환경적으로 처리하고 간편하게 처리함으로써 수질 및 토양오염 등으로 인한 환경오염의 원인을 방지하고 고 유가시대에 있어 에너지를 만들어 회수하여 사용하고 처리된 잔재 물은 다시 액비 또는 고형 퇴비화 공정으로 이송되어 다시 사람들의 먹거리의 영양소로 공급되는 완벽한 무한 재활용에너지원이다.  Such organic waste multi-digestion treatment method of the independent facility of the present invention is more environmentally friendly and easily treated using the organic waste and animal husbandry ingredients that are essential to the process of people's lives, resulting in water and soil pollution, etc. Preventing the causes of environmental pollution, creating and recovering energy for high oil prices, the processed remnants are transferred to the liquid fertilizer or solid composting process, which is the perfect endless recycled energy source that is supplied to the nutrients of people's food.

또한 최초 통성협기성균을 접종시킬 때 기존 방법은 종균을 직접 투여하여 수천만원의 비용이 들어가고 한번의 종균 접종으로 안정화를 보장 못해 잘못될 경우 지속적으로 접종비용이 발생된다.In addition, when inoculating the first communicable strains, the existing method directly costs the cost of tens of millions of dollars by directly administering the seed, and once the seed is inoculated, it cannot guarantee the stabilization.

본발명 중 최초 접종시 톱밥, 쌀겨등 무기물과 닭의 배설물을 섞어 처리하고자 하는 유기물질과 함께 고안한 소화시스템에 투여하여 일정기간을 숙성 발효하면 추천만원의 종균비용 절감과 무기물이 단계별 소화조에 잔류하여 통성협기성균의 활발한 증식과 메탄가스 즉 바이오가스 또한 기존의 방법보다 보다 많은 생산성을 갖는다.During the first inoculation of the present invention, the minerals such as sawdust and rice bran are mixed with the organic material to be treated with the organic material to be treated, and then fermented for a certain period of time. Therefore, active growth of communicable strains and methane gas, that is, biogas, also have more productivity than conventional methods.

이하, 본 발명의 독립시설물의 유기성폐기물다중 처리방법을 첨부도면을 참조하여 설명하면 다음과 같다.  Hereinafter, the organic waste multiple treatment method of the independent facility of the present invention will be described with reference to the accompanying drawings.

도 1은 본 발명의 실시예의 유기성폐기물의 다중처리를 위한 시스템의 일예이고, 도 2는 본 발명의 유기성폐기물의 단계별 독립적소화되어 최종배출되는 흐름도이고, 도3은 전체 유기성폐기물의 처리에 대한 플로우차트이다.1 is an example of a system for the multiple treatment of organic waste of the embodiment of the present invention, Figure 2 is a flow chart of the step-by-step independent digestion and final discharge of the organic waste of the present invention, Figure 3 is a flow for the treatment of the entire organic waste It is a chart.

유기성폐기물이 투입구(50)를 통하여 1차 교반 및 협기성균에 의해 최적의 유기물질 분해를 하기위한 유기물을 도2의 파쇄기(70)를 통해 파쇄하고, 유기물질 외의 고형물을 내부에 통성 혐기성균의 작용에 의해 단계별로 발효되게 개구부(30H)통하기 전 비 유기물질 걸음장치(10)과 비유기물질을 바깥으로 배출하는 배출스크류(11)를 통하여 배출한다.The organic waste is crushed through the inlet 50 through the crusher 70 of FIG. 2 for the optimal decomposition of organic matter by primary agitation and anaerobic bacteria, and solids other than organic matter are collected inside of the anaerobic bacteria. Before passing through the opening (30H) step by step by the action is discharged through the non-organic material step device 10 and the discharge screw 11 for discharging the non-organic material to the outside.

외부로 배출된 배출물은 유기물과 비유기물로 한번 더 분류되어 자원화 할 수 있는 유기물질은 소화시스템의 투입구(50)으로 유기물이송관(54)을 통해 다시 투입되고, 소화스시템에 의한 소화가 안되는 비 유기물질은 분리 작업하여 분리 폐기한다.Emissions discharged to the outside are once again classified into organic and non-organic materials, and the organic materials that can be recycled are re-injected through the organic transport pipe 54 to the inlet 50 of the digestive system, and are not digested by the extinguishing system. Non-organic materials are separated and disposed of.

소화시스템의 완전한 소화 및 에너지자원화를 위하여 내부공간을 소화특징별 구획하는 있어 다섯개의 격벽(31)(32)(33)(34)(35)이 소정의 간격으로 형성되어 있고, 각 격벽의 하부측에는 유기물질이 각 소화실별로 이동, 통로기능을 하게 되는 개구부 개폐장치(30H)(31H)(35H)와 소화가 완료된 알카리발효 및 액비저장조(46)에서 액비퇴비화 배출구(53)을 통하여 액비가 다음 퇴비화장치로 배출되면 개구부(30H)(31H)(35H)가 순차적으로 열여 유기물질이 각각의 소화실로 통하는데 이는 유기물질 자연흐름 경사면(57)의 원리로 동력을 사용하지 안고 자연적으로 흘러내리도록 하향으로 기울어지게 되어있고, 또한 개구부개폐장치((30H)(31H)(35H)없는 각각의 소화실 격벽은 도2 와같이 일정한 소정의 간격을 두어 유기물질이 도2의 유기물질 흐름방향(60)(61)(62)(63)(64)과 같이 자연적 순환흐름으로 흐름의 길이를 최대화하여 각각의 소화실에서 완벽한 소화분해를 촉진하고 혐기성균의 왕성한 활동을 보장하며, 순차적으로 산성발효소(41)에서 산성저하조(42)(43)(44)(45) 거쳐 알카리발효 및 액비저장조(46)까지 산성의 PH를 알카라리로 떨어트린다.Five partitions 31, 32, 33, 34, and 35 are formed at predetermined intervals to partition the internal space according to the extinguishing characteristics for complete extinguishing of fire extinguishing system and energy resources. On the side, the liquid matter is discharged through the liquid composting discharge port 53 in the alkaline fermentation and liquid fertilizer storage tank 46 and the opening and closing device 30H, 31H, 35H, in which organic substances move and pass through each fire extinguishing chamber. When discharged to the composting device, openings 30H, 31H, and 35H are sequentially opened, and organic materials pass through each fire chamber, which flows naturally without using power on the principle of the organic material natural flow slope 57. It is inclined downward so as to be inclined downward, and each fire compartment partition wall without the opening / closing device (30H, 31H, 35H) is spaced at a predetermined interval as shown in FIG. Like 60) (61) (62) (63) (64) The continuous circulation flow maximizes the length of the flow to promote complete digestion in each digestion chamber and to ensure vigorous activity of the anaerobic bacteria, and sequentially to acid lowering enzymes (42) (43) (44). (45) The acidic pH is dropped into the alkaline fermentation to the alkaline fermentation and liquid fermentation tank (46).

최초 혐기성균 및 혐기성균의 왕성한 활동의 조건을 만들어주기 위하여 접종시 산성발효조(41)에는 유기물질의 주성분을 이루는 고분자의 유기물을 미생물의 소화활동에 의해 저분자의 유기물로 발효되게 하는 통성 혐기성균을 촉진시키고 바이오가스 생산량을 늘릴 수 있는 톱밥, 쌀겨, 파쇄된 마른풀 등 과 같은 무기물질과 양계장에서 배출되는 계분을 8대2로 적절하게 섞어 기타 처리할 유기성폐기물과 함께 유기물 70%, 통성혐기성균 촉진무기물30%를 투입하여 일정기간 혐기성균을 증가시고 황성한 활동을 보장 시킨다.In order to make the conditions of active activity of the first anaerobic bacteria and anaerobic bacteria, the acidic fermentation tank (41) at the time of inoculation has a fermentable anaerobic bacteria which ferments the organic material of the polymer constituting the main component of the organic material into the low molecular weight organic material by the digestion activity of the microorganism. Inorganic materials such as sawdust, rice bran, crushed dry grass, etc. and poultry discharged from poultry farms can be mixed 8 to 2 properly to promote biogas production. 30% of promoted minerals are added to increase anaerobic bacteria for a certain period of time, and ensure the activity of abundance.

이는 자연상테에서 친환경적으로 촉진제 역할을 하고 더 나아가 기존 방식인 최초 협기성균 접종비용 수천만원을 절약하는 이익도 있다.This also serves as an environmentally friendly promoter in the natural environment and further saves tens of millions of won of the initial method of inoculation.

시스템 내부 일측에는 저장발효되는 유기물질 시간의 경과에 의해 응고 또는 침전되는 현상을 방지하기 위하여 교반기(20(21)(22)의 간헐적으로 동작시킨다.One side of the system is operated intermittently in the stirrer (20 (21) 22) to prevent the phenomenon of solidification or precipitation by the passage of the storage of the organic material time.

유입된 유기물질의 지방산을 더욱 분해시켜 농도를 물게 하면서 1차산성발효조(41)및 2차산성발효조(42), 3차산성발효저하조(43), 4차산성발효저하조(44)에서 각각의 혐기성균에 의해 소화되는 과정 중 발생되는 메탄가스 즉 바이오가스가 생성되며, 이 바이오가스는 공기보다 밀도가 낮아 위로 오르는 힘을 가지고 있어 공기중 응집된 물흐름 경사면(58)을 타고 올라가 1차산성발효조(41)의 바이오가스포집구멍(51H)과 2차산성발효조부터 5차산성저하발효조(45)에서 생성된 바이오가스는 공기중 응집된 물 흐름경사면(58)을 타고 올라가 2차산성발효조의(42)의 바이오가스포집구멍(51H)을 통과하여 바이오가스배출구(51)를 통과하여 바이오가스 포집탱크 등의 바이오 가스 처리 플랜트 부분으로 이송된다.In the primary acid fermentation tank (41) and the secondary acid fermentation tank (42), the tertiary acid fermentation lowering tank (43), and the fourth acid fermentation lowering tank (44) while further decomposing the fatty acid of the introduced organic material to make the concentration bite. Methane gas, or biogas, generated during the digestion process by each anaerobic bacteria is generated, and the biogas is less dense than air and has a force of rising upward. The biogas generated from the biogas spout hole 51H and the secondary acid fermentation tank 45 of the primary acid fermentation tank 41 and the secondary acid lowering fermentation tank 45 are taken up on the condensed water flow slope 58 in the air to be secondary acid. It passes through the biogas capture hole 51H of the fermentation tank 42, passes through the biogas discharge port 51, and is conveyed to the biogas processing plant part, such as a biogas collection tank.

이때, 기온이 낮은 동절기의 경우 미생물의 활동을 활성화시키기 위해 각각의 발효조에는 바이오가스를 이용한 열병합발전에서 생산되는 열을 일부 나누어 소화시스템 전체에 도2 난방배관(59)을 사용하여 일정온도 중온35도~38도로 유지하고 산성도(pH) 조정기 등을 설치하여 최적의 소화시스템을 유지시킨다.At this time, in order to activate the activity of microorganisms in the winter when the temperature is low, each fermentation tank divides the heat produced by the cogeneration system using biogas, and uses the heating pipe 59 of FIG. Maintain an optimal digestion system by maintaining a temperature of 38 ~ 38 degrees and installing an acidity regulator.

한편, 유기물질 자연흐름경사면(57)의 경사하부측에 위치한 알카리성발효조(46)는 상기 발효과정을 통해 알카리성을 띤 액체 형태로 변화된 소위 액비를 수용하게 되며, 그 상측에 설치된 액비 배출구 및 접안확인 구(53)를 통해 저장된 액비의 슬러지화를 감응하여 미생물의소화활동에 최적의 조건을 유지하게 한다.On the other hand, the alkaline fermentation tank 46 located on the lower side of the slope of the organic material natural flow slope 57 accommodates the so-called liquid fertilizer changed into an alkaline liquid form through the fermentation process, the liquid fertilizer outlet and eyepiece installed on the upper side Through the sphere (53) to react the sludge of the stored liquid fertilizer to maintain the optimum conditions for the digestion activity of the microorganisms.

액비 배출구 및 접안확인구(53)는 투명한 강화유리 덮개로 만들어지며 평상시에는 잠겨있어 냄새를 배출하지 않는다.The liquid rain outlet and the eyepiece confirmation port 53 is made of a transparent tempered glass cover and is normally locked so as not to emit odors.

도 1은 본 발명의 실시예의 유기물질처리를 위한 처리시스템의 전체구성도, 도 2는 본 발명의 유기성물질의 투입부터 배출까지의 유기물질의 흐름등 을 볼수 있는 평면도, 도3은 처리방법에 대한 플로우차트이다.  1 is an overall configuration diagram of a processing system for organic material treatment according to an embodiment of the present invention, Figure 2 is a plan view of the flow of the organic material from the input to the discharge of the organic material of the present invention, Figure 3 is a treatment method Is a flowchart.

< 도면의 주요부분에 대한 부호의 설명><Description of reference numerals for main parts of the drawings>

10 : 유기물외 불순물거름장치, 11 : 물순물배출스크류10: impurity filtering device other than organic matter, 11: water pure water discharge screw

20, 21, 22 : 교반기, 30, 31, 32, 33, 34, 35 : 격벽20, 21, 22: agitator, 30, 31, 32, 33, 34, 35: bulkhead

30H, 31H, 35H : 개구분 개패장치30H, 31H, 35H: Opening and closing device

40, 40T : 원료1차교반 및 불순물제거조, 41, 41T : 1차산성발효조40, 40T: Primary stirring and raw material removal tank, 41, 41T: Primary acid fermentation tank

42, 42T : 2차산성발효조, 43, 43T : 3차산성발효저하조, 44, 44T : 4차산성발효저하조, 42, 42T: secondary acidic fermentation tank, 43, 43T: tertiary acid fermentation lowering tank, 44, 44T: quaternary acidic fermentation lowering tank,

45, 45T : 5차산성발효저하조, 46, 46T : 알카리성발효조45, 45T: 5th acidic fermentation tank, 46, 46T: alkaline fermentation tank

50, 50H : 투입구, 51, 51U : 바이오가스배출구50, 50H: inlet, 51, 51U: biogas outlet

53 : 액비배출구 및 접안확인구, 54 : 유기성폐기잔제물이송53: liquid discharge outlet and eyepiece confirmation port, 54: transfer of organic waste residue

51H : 바이오가스포집구멍, 57 : 유기물질자연흐름경사면51H: Biogasfoam hole, 57: Natural flow slope

58 : 공기중 응집된 물 흐름경사면58: inclined water flow slope in air

60, 61, 62, 63, 64 : 유기물질흐름방향60, 61, 62, 63, 64: organic material flow direction

70 : 파쇄기70: shredder

Claims (1)

청구항 1.  Claim 1. 유기성폐기물 즉 유기물질을 저장, 파쇄, 부터 소화, 가스배출 및 액비 배출 까지의 모든 공정이 하나의 시스템으로 운영되는 방법 및 장치.A method and apparatus in which all processes from organic waste, ie, organic matter, to storage, crushing, digestion, gas discharge and liquid discharge are operated in one system. 청구항 2.Claim 2. 원료1차교반 및 불순물제거조(40)에서 원료교반 및 동시에 유기물질을 5mm이하로 파쇄하는 장치와 유기성물질이 아닌 불순물을 거르는 장치 및 저 장조.In the raw material primary stirring and impurity removal tank 40, the raw material stirring and at the same time the device for crushing the organic material less than 5mm and the device for filtering impurities and storage of non-organic material. 청구항 3.Claim 3. 원료1차교반 및 불순물제거조(40)와 2차산성발효조부터 5차산성저하조(45) 상부에 설치된 각각의 공기중 응집된 물 흐름경사면(58)을 이용하여 응집된 물 즉 이슬을 소화조 내부로 경사에 의해 자연적으로 흘려 보내고 비증이 낮은 메탄가스 즉 바이오가스는 경사면을 타고 쉽게 올라가 바이오가스포집구멍(50H)로 자연적으로 올라가는 장치 및 시설Coagulated water, that is, dew, using the agglomerated water flow slope 58 of each air installed on the raw material primary stirring and impurity removal tank 40 and the secondary acidic fermentation tank to the fifth acidic acid lowering tank 45, respectively. The device and facility that naturally flows by the slope to the inside, and low methane gas, or biogas, climbs easily on the slope and naturally rises to the biogas spout hole (50H). 청구항 4.Claim 4. 액비배출구 및 접안확인구(53)에서 알카리성발효조(46)있는 액비가 배출될 때 격벽(35)에 있는 개구부(35H)는 원격자동 또는 수동으로 닫혀있고 각각의 격벽(30)(31)(32)When the liquid fertilizer with alkaline fermentation tank 46 is discharged from the liquid fertilizer discharge port and the eyepiece confirmation port 53, the opening 35H in the partition 35 is remotely or manually closed and each of the partition walls 30, 31 and 32 ) (33(34(35)을 유기물질이 통과할 때 격벽(30)의 개구부(30H)(31H)는 원격자동 또는 수동으로 순차적으로 열려 원료1차교반 및 불순물제거조 에서부터(41)(Openings 30H and 31H of the partition 30 when the organic material passes through 33 (34 (35)) are sequentially opened remotely or manually from the raw material primary stirring and impurity removal tank (41) (42)(43)(44)(45)(46)으로 까지 유기물질자연흐름 경사면(57)을 타고 흐는 방법 및 장치(42) (43) (44) (45) (46) Method and apparatus for flowing on the organic material natural flow slope 57 청구항 5. Claim 5. 각각의 소화조에 있는 각각의 격벽(31)(32)(33)(34)은 도2와 같이 서로 상이하게 유기물질이 이동할 수 있는 통로를 만들어 유기물질이 최대한 천천히 흐르면서 소화되도록 내벽과 이격 둔 통로를 만드는 방법Each of the partition walls 31, 32, 33, 34 in each digester creates a passage through which organic materials can move differently from each other, as shown in FIG. How to make 청구항 6.Claim 6. 제6항에 있어서 협기성균의 왕성한 활동을 보장하고 초식동물의 되새김질 하는 소화 방법을 응용 소화시스템 구획을 총6곳으로 나누어 소화시간을 최대화시켜 완전 소화하 및 바이오가스의 생산량을 최대화 생산하는 방법.7. The method according to claim 6, wherein the digestive method of ensuring the active activity of the anaerobic bacteria and the rubbing of the herbivore is divided into a total of six application digestive system sections to maximize the digestion time and maximize the production of the complete digestion and biogas production. 청구항 7.Claim 7. 제5항, 제6항에 있어 협기성균의 빠른 증식과 바이오가스의 높은 생산성을 위하여 최초 유기물질 투입시 톱밥, 쌀겨, 파쇄된초지풀 등의 무기물과 닭의 배설물 즉 계분을 섞어 투입되는 유기물성폐기물 즉 처리하고자 하는 음식물쓰레기,축산분뇨 등을 7할과 무기물3할을 함께 투입하여 일정기간 숙성시켜 자연적으로 협기성균을 촉진시키고, 바이오가스생산을 증대시키는 방법 The organic material of claim 5 and 6, wherein inorganic substances such as sawdust, rice bran, and crushed grass paste are mixed with chicken excrement, that is, poultry powder, for the first time in order to increase the growth of anaerobic bacteria and high productivity of biogas. Waste, that is, food waste and livestock manure to be treated, and 70% and inorganic 30% are aged together for a certain period of time to naturally promote anaerobic bacteria and increase biogas production. 청구항 8.Claim 8. 제1항에 있어서 동력이 없어도 독립적으로 유기물질 자연흐름경사면(57)을 이용하여 각각의 격벽을 거쳐 유기물질이 흘러 완전 소화하는 무동력소화시스템 및 처리방법The non-powered fire extinguishing system and treatment method according to claim 1, wherein the organic material flows through each partition wall and is completely extinguished using the organic material natural flow slope 57 without power.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101151557B1 (en) * 2011-11-14 2012-05-30 전남대학교산학협력단 Dry anaerobic digestion chamber
KR101313766B1 (en) * 2013-01-18 2013-10-01 주식회사 신영그린시스 Apparatus and method for high-performance anaerobic digestion using mixture of livestock wastewater and subsidiary materials
CN110028204A (en) * 2019-05-22 2019-07-19 中国农业大学烟台研究院 A kind of quick anaerobic fermentation system of livestock and poultry liquid dung

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101151557B1 (en) * 2011-11-14 2012-05-30 전남대학교산학협력단 Dry anaerobic digestion chamber
KR101313766B1 (en) * 2013-01-18 2013-10-01 주식회사 신영그린시스 Apparatus and method for high-performance anaerobic digestion using mixture of livestock wastewater and subsidiary materials
CN110028204A (en) * 2019-05-22 2019-07-19 中国农业大学烟台研究院 A kind of quick anaerobic fermentation system of livestock and poultry liquid dung

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