KR20120105182A - Manufacturing method of organic compost - Google Patents

Manufacturing method of organic compost Download PDF

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KR20120105182A
KR20120105182A KR20110022841A KR20110022841A KR20120105182A KR 20120105182 A KR20120105182 A KR 20120105182A KR 20110022841 A KR20110022841 A KR 20110022841A KR 20110022841 A KR20110022841 A KR 20110022841A KR 20120105182 A KR20120105182 A KR 20120105182A
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mixture
organic
mixing
quicklime
organic waste
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KR20110022841A
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KR101227377B1 (en
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박종철
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주식회사 햇토비
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00Other organic fertilisers
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D3/00Calcareous fertilisers
    • C05D3/02Calcareous fertilisers from limestone, calcium carbonate, calcium hydrate, slaked lime, calcium oxide, waste calcium products
    • 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
    • C05F17/50Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
    • 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
    • C05F17/60Heating or cooling during the treatment
    • 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
    • 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
    • C05G5/00Fertilisers characterised by their form
    • C05G5/30Layered or coated, e.g. dust-preventing coatings
    • C05G5/35Capsules, e.g. core-shell
    • 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

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Pest Control & Pesticides (AREA)
  • Inorganic Chemistry (AREA)
  • Fertilizers (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE: A manufacturing method of organic material compost is provided to increase contents of organic material in organic waste and to enhance compost maturity. CONSTITUTION: A manufacturing method of organic compost comprises the following steps: removing and pulverizing organic waste; respectively controlling amount of contained water in livestock excretions and organic waste; creating a first mixture by mixing 70wt% of the organic waste with 30wt% of livestock excretion in a mixing reactor; creating a second mixture by mixing 10-20 quicklime based on 100 wt% of the first mixture; processing a first sterilization and solid material pulverization; creating a third mixture by mixing 30-50 wt% of slow-releasing by-product raw material based on 100wt% of the second mixture; processing the rotten fermentation; and drying the third mixture at a mixing field. [Reference numerals] (1) Organic waste; (2) Animal feces; (AA) Manufacturing process; (BB) Drying path; (CC) Control the water content as 50-60% in the drying path; (DD) Control the water content as 60-70% in the drying path; (EE) Injection; (FF) Mixing reactor; (GG) Injection; (HH) First mixture; (II) Quick lime; (JJ) Second mixture; (KK) Third mixture; (LL) Completed by-products; (MM) Oxygen supply; (NN) Leachat spray; (OO) Drying at an agitator; (PP) Packing

Description

유기질 퇴비의 제조방법 {Manufacturing method of organic compost} Manufacturing method of organic compost {Manufacturing method of organic compost}

본 발명은 동물성 및 식물성 잔재물 예컨대 음식물쓰레기, 농축산물의 폐기물 등 유기성폐기물과 가축분뇨등을 혼합발효조에 투입하여 혼합한 1차혼합물에 다시 생석회를 투입하여 균일하게 혼합한 2차혼합물을 조성한 다음, 상기 2차혼합물에 가공된 버섯베이지(버섯재배용 포트에 잔재 된 톱밥과 버섯 부스러기) 팜박(야자수껍데기 등 잔재물), 단미사료박(단미사료 제조시 폐기물), 당박(설탕제조시 사탕수수찌꺼기 및 설탕슬러지등)등 완효성 부산물원료를 투입하여 3차혼합물을 조성하여 일정기간 부숙발효공정을 거쳐서 교반장으로 배출하여 건조공정을 거침으로서 유기물의 함유량을 높힘과 동시에 부숙도를 높이는 것을 특징으로 하는 유기질 퇴비의 제조방법에 관한 것이다.In the present invention, the organic and vegetable residues such as food waste and agricultural wastes, organic waste and livestock manure, etc. are added to the mixed fermentation tank, and the lime is added to the mixed first mixture to form a second mixture that is uniformly mixed. Mushroom Beige (sawdust and mushroom crumbs left in the mushroom cultivation pot) palm bak (remains such as coconut shells), sweet rice flakes (waste for making sweet feeds), sorghum (sugarcane flakes and sugar sludge for sugar production) Etc.) The tertiary mixture is prepared by adding the slow-by-product by-products and discharged to the agitation station after a certain period of fermentation process for drying for a period of time to increase organic matter content and increase maturity. It relates to a manufacturing method.

일반적으로 동, 식물성 잔재물이나 가죽분뇨등과 같은 유기성폐기물을 이용하여 유기질 퇴비를 제조하는 방법은 유기성폐기물의 수분을 조절한 다음 생석회와 혼합하여 산화소성반응을 시키고, 산화소성 과정 중에 가수분해 및 중금속제거, 염분의 감속의 화학적 반응을 거쳐서 건조하도록 되어 있었다.In general, organic compost using organic waste such as copper, vegetable residues or leather manure is produced by controlling the moisture of organic waste and then mixing it with quicklime to undergo oxidative reaction, and hydrolysis and heavy metal during oxidative process. It was made to dry through the chemical reaction of removal and deceleration of salt.

즉 유기성폐기물과 산화소성 반응제의 반응을 보면,In other words, the reaction of organic waste and oxidizing reactant,

① Ca0 + H₂0 (폐기물중의물) → Ca(0H)₂ + 15 Kcal/mo1       ① Ca0 + H₂0 (water in the waste) → Ca (0H) ₂ + 15 Kcal / mo1

② Mgo + H₂0 (폐기물중의물) → Mgo(0H)₂ + 15 Kcal/mo1       ② Mgo + H₂0 (water in the waste) → Mgo (0H) ₂ + 15 Kcal / mo1

이때 폐기물 중의 물과 산화칼슘 및 산화마그네슘은 발열반응으로 동식물성 잔재물과 가축분뇨 등의 혼합물인 유기성폐기물을 발효조 내에서 평균 100도C 까지 온도가 상승하여 산화소성 시키게 된다. 이때 상기 유기성폐기물에 함유되어 있는 염분은 적량의 생석회를 투입하여 혼합하면 아래와 같은 화학반응을 하게 된다.At this time, the water, calcium oxide, and magnesium oxide in the waste are exothermic to cause the organic waste, which is a mixture of animal and plant residues and livestock manure, to rise to an average temperature of 100 ° C in the fermenter to oxidize. At this time, the salt contained in the organic waste is mixed with an appropriate amount of quicklime to perform the following chemical reaction.

③ NaC1 + CaS0₄→ CaC1₂ + Na₂S0₄        ③ NaC1 + CaS0₄ → CaC1₂ + Na₂S0₄

위와 같은 반응식에 의해 대부분 제거되는 것은 널리 공지된 사실이다.It is well known that most of the reactions are eliminated by the above reaction scheme.

상기와 같은 ③의 반응식에 의하여 동, 식물성 잔재물과 같은 유기성폐기물에 생석회를 균일하게 혼합하여 유기질 퇴비를 제조하게 되는데, 종래의 기능성 복합비료를 제조하는 방법은 상기 유기질 퇴비를 제조하는 공정중에 식물성장에 필수적, 필요한 3대 원소인 질소(N), 인산(P), 가리(K)를 일부 소멸시키게 되는 생석회를 과다 사용하였고, 과다한 생석회의 투여로 인하여 상기 유기질 퇴비의 부숙도가 충분하지 못하게 되어 암모니아 가스가 다량 발생함으로써 잎, 줄기가 마르게 되어 작물의 성장에 피해를 입게 되는 결점이 있었다.According to the reaction formula of ③ as described above to produce organic compost by uniformly mixing quicklime with organic waste, such as copper and vegetable residues, the conventional method for producing a functional compound fertilizer plant growth during the process of manufacturing the organic compost Excessive use of quicklime, which will partially dissipate the necessary three major elements, nitrogen (N), phosphoric acid (P), and girly (K), has caused the organic compost maturity to become insufficient due to the excessive amount of quicklime. The large amount of ammonia gas caused the leaves and stems to dry out, which caused damage to crop growth.

즉, 부숙도가 낮은 퇴비나 화학비료를 유기성폐기물과 함께 생석회를 혼합기에 투입하여 단시간 내에 기능성 복합비료를 제조하였기 때문에 석회질의 과다한 투여로 식물성장에 필요한 3대 원소인 질소, 인산, 가리를 일부 소멸시키고, 상기 유기성퇴비의 부숙도가 낮게 되며, 또한 불필요하게 과다한 생석회의 투여로 상기 기능성 복합비료를 시비할 경우 화학반응으로 인하여 다량의 암모니아가스가 발생하게 되어 입, 줄기가 누렇게 마르게 되어 작물의 성장에 피해를 주게 되었다.In other words, since compost or chemical fertilizer with low maturity was added to organic mixers with quicklime, a functional complex fertilizer was prepared within a short time. When the organic compost fertilizes, the maturity of the organic compost becomes low, and when the functional compound fertilizer is fertilized unnecessarily by the administration of excessive lime, a large amount of ammonia gas is generated due to a chemical reaction, resulting in a yellowing of the mouth and stems. The growth was damaged.

특히 석회질 비료는 토양개량에는 뛰어난 효과가 있으나, 질소비료(요소, 유안)가 토양에서 혼합되면 암모니아 이온이 발생되고, 토양속의 암모늄 이온은 석회질비료와 만나면 화학반응을 일으켜서 다량의 암모니아 가스가 발생하여 식물(작물) 아랫부분에서 윗부분까지 잎과 줄기가 누렇게 타서 녹아내리는 등 큰 피해를 주게 된다.In particular, calcareous fertilizer has an excellent effect on soil improvement, but when nitrogen fertilizer (urea, yuan) is mixed in soil, ammonia ions are generated, and ammonium ions in the soil cause chemical reactions when they meet with calcareous fertilizer. From the bottom of the plant (crop) to the top, leaves and stems burn yellow and melt, causing great damage.

또한, 음식물쓰레기 등의 유기성폐기물과 생석회를 혼합하여 유기질비료를 제조하는 방법은 한국등록특허공보(공고일 일자 2007. 12. 27, 등록번호 10-0788243)에 소개되고 있으나, (위 특허는 본원발명자 겸 출원인인 박종철이 발명한 것임), 한국특허 제10-0788243호의 제조방법으로 제조된 유기질비료는 유기물함량이 공정규격에 비하여 25% 이하가 되고, 부숙도 역시 70 이하로 되어 유기질 퇴비로서 규격미달이 되어 상품성이 없으므로 현재 제조를 중지하게 되었다.In addition, a method for manufacturing organic fertilizer by mixing organic waste such as food waste and quicklime is introduced in Korea Patent Publication (Dec. 27, 2007, Registration No. 10-0788243), but the above patent is the inventor of the present invention The organic fertilizer prepared by the method of the present invention and patent applicant Park Jong-cheol), Korean Patent No. 10-0788243 has an organic matter content of 25% or less compared to the process standard, and the maturity is also 70 or less, which is less than an organic compost. As it is not commercially available, the current production is discontinued.

이러한 종래의 기술(한국특허공보(공고일자 2007. 12. 27) 즉, 음식물쓰레기 등의 유기성폐기물과 생석회를 혼합한 유기질비료는 유기물함량이 공정규격에 비하여 25% 이하가 되고, 부숙도 역시 70 이하가 되어 유기질 퇴비로서 규격이 미달 되었기 때문에 이러한 결점을 해결하기 위하여, 동,식물성 잔재물로 구성된 유기성폐기물과 축산분뇨의 수분함량을 각각 조절한 후, 혼합반응조내에 투입하여 유기성폐기물(1)과 가축분뇨(2)를 균일하게 혼합한 혼합물(3)(이하 "1차혼합물"이라 약칭함)을 조성하고, 상기 1차혼합물(3)에 적량의 생석회(4)를 투입한 후, 균일하게 혼합하여 2차혼합물(5)을 조성한 다음, 상기 2차혼합물(5)에 가공된 버섯베이지, 팜박, 단미사료박, 당박으로 구성된 완효성부산물원료(6)를 투입하여 균일하게 혼합한 3차혼합물(7)을 조성하여 일정기간 부숙발효공정을 거쳐서 건조시킴으로서 유기물의 함유량을 높이고 동시에 부숙도를 높힌 유기질 퇴비의 제조방법을 제공하는데 본 발명의 목적이 있다.Such conventional technology (Korean Patent Publication (Dec. 27, 2007), that is, organic fertilizer mixed with organic waste such as food waste and quicklime, the organic matter content is less than 25% compared to the process standard, the maturity is also 70 In order to solve these drawbacks, the organic waste composed of animal and plant residues and livestock manure were respectively regulated, and then the organic waste (1) and livestock were put into a mixed reaction tank. A mixture 3 (hereinafter abbreviated as " primary mixture ") obtained by uniformly mixing the manure 2 is formed, and an appropriate amount of quicklime 4 is added to the primary mixture 3, followed by uniform mixing. To form a secondary mixture (5), and then into the secondary mixture (5), a tertiary mixture (10) consisting of a processed mushroom beige, palm foil, sweet rice cake, and sugar lysate, which was then uniformly mixed ( 7) by working Period decomposed through a fermentation process to increase the content of organic matter has a dry sikimeuroseo at the same time an object of the present invention to provide a method of manufacturing the organic compost nophin the compost FIG.

따라서 본 발명은 상기와 같은 제반문제점을 해결하기 위하여 창출한 것으로, 동, 식물성잔재물로 구성된 유기성폐기물(1)과 축산분뇨(2)의 수분함량을 각각 조절한 후, 혼합반응조(M)에 투입하여 1차혼합물(3)을 조성하고, 상기 1차혼합물(3)에 적량의 생석회(4)를 투입하여 균일하게 혼합한 2차혼합물(5)을 조성하여, 상기 2차혼합물(5)의 표면에 생석회(4)가 코팅되면서 2차혼합물(5)의 온도가 100도C 내지 120도C 상승되어 1차 살균, 멸균 및 고형물질의 분해 안정화 공정을 거친 다음, 혼합반응조(M)내의 상기 2차혼합물(5)에 완효성부산물원료(6)를 투입하여 상기 2차혼합물(5)과 균일하게 혼합하여 3차혼합물(7)을 조성하여 일정기간 부숙발효공정을 거쳐서 건조시킴으로서 질소, 인산, 가리등 유기물의 함유량을 높여줌과 동시에, 부숙도를 높일 수 있고, 상기 3차혼합물(7)의 부숙과정에서 2차 살균, 멸균 및 고형물질의 분해, 안정화공정을 거치게되며, 상기 3차혼합물(7)의 부숙 발효과정에서 혼합반응조(M)내에서 발생하는 침출수를 따로 분리하여 투기처분하지 않고, 상기 혼합반응조(M)내의 3차혼합물(7)에 1일 2~4회 분사하여 줌으로서 친환경적인 유기질퇴비의 제조방법을 창출하였다.Therefore, the present invention was created to solve the above problems, and after adjusting the water content of the organic waste (1) and livestock manure (2) consisting of copper, vegetable residues, respectively, and put into the mixed reaction tank (M) To prepare a primary mixture (3), and to add the appropriate amount of quicklime (4) to the primary mixture (3) to form a secondary mixture (5) uniformly mixed, the secondary mixture (5) As the quicklime 4 is coated on the surface, the temperature of the secondary mixture 5 is increased to 100 ° C. to 120 ° C., followed by primary sterilization, sterilization, and decomposition stabilization of solid materials. Slowly adding by-product active material (6) to the secondary mixture (5) and uniformly mixed with the secondary mixture (5) to form a tertiary mixture (7) by drying through a period of maturity fermentation process, nitrogen, phosphoric acid, girly It is possible to increase the organic content of the back, and at the same time increase the maturity, Secondary sterilization, sterilization and decomposition and stabilization of solid materials are performed during the mixing of the mixture (7), and the leachate generated in the mixed reaction tank (M) is separated separately during the ripening of the tertiary mixture (7). By spraying twice or four times a day to the tertiary mixture (7) in the mixing reactor (M) without dumping, creating an environmentally friendly method for producing organic compost.

본원 발명은 유기성폐기물과 가축분뇨의 수분함량을 적정하게 조절하여 혼합한 1차혼합물에 적량의 생석회를 투여하여 균일하게 혼합한 2차혼합물에 적량의 완효성 부산물원료를 투여하여 혼합하여 3차혼합물을 조성하여 혼합안정화공정을 거쳐서 유기물(완효성 부산물원료)을 보충함으로써, 유기물의 함량을 높이고 동시에 3차혼합물을 혼합반응조내에서 일정기간(10일 내지 15일간)부숙발효공정을 거치게 되므로 부숙발효를 효과적으로 실시하여 부숙도를 높이는 작용효과가 있고, 또한 상기 혼합발효조에서 발생하는 유기성폐기물의 침출수를 따로 분리하여 투기처분하지 않고 상기 혼합발효조내의 3차혼합물에 1일 2~4회 분사하여 부숙발효를 원활하게 하게 되므로 친환경적인 유기질 퇴비를 제조할 수 있는 효과를 갖는다.According to the present invention, a third mixture is prepared by administering an appropriate amount of slow-acting by-products to a second mixture that is uniformly mixed by administering an appropriate amount of quicklime to the first mixture, which is appropriately controlled by controlling the moisture content of organic waste and livestock manure. By replenishing organic matter (finished by-product raw material) through the composition stabilization process, the organic matter content is increased and at the same time, the tertiary mixture is subjected to a fermentation process for a period of time (10 to 15 days) in the mixing reactor to effectively ferment the fermentation. It is effective to increase the maturity, and also to separate the leachate of organic wastes generated in the mixed fermentation tank separately and sprayed to the tertiary mixture in the mixed fermentation tank 2 to 4 times a day without sedimentation and smooth fermentation fermentation. Since it will be an environmentally friendly organic compost has the effect to produce.

도1 은 제조공정도임1 is a manufacturing process diagram

본 발명은 동, 식물성 잔재물로 구성된 유기성폐기물에서 이물질(예컨대, 플라스틱, 비닐지, 금속 등)을 제거하고 분쇄하는 선별분쇄하는 공정을 거쳐서, 건조로내에 각각 투입하여 상기 유기성폐기물(1)의 수분함량을 50% ~ 60%로 조절하고, 가축분뇨(2)는 수분함량 60% ~ 70%로 조절하게 되는데, 상기 가축분뇨의 수분함량을 60% ~ 70%로 조절하는것은 상기 가축분뇨(2)의 비료성분중 휘발성성분의 손실을 방지하고저 하는것으로, 상기 유기성폐기물(1) 70중량%와 가축분뇨(2) 30중량%를 혼합반응조(M)에 투입하여 균일하게 혼합한, 1차혼합물(3)을 조성한 다음, 혼합반응조(M)내에서 상기 1차혼합물(3)에 100중량%에 대하여 생석회(4) 10중량% 내지 20중량%를 서서히 투여하여 균일하게 혼합한 2차혼합물(5)을 조성하여, 상기 2차혼합물(5)의 표면에 생석회(4)가 코팅되면서 2차혼합물(5)의 온도가 100도C ~ 120도C 정도에서 1차 살균, 멸균 및 고정물질의 분해로 안정화하는 공정을 거치게 되는데, 이 경우 2차혼합물(5)은 유기물 함량이 공정규격에 비하여 현저하게 낮은 25% 이하가 되고, 부숙도 역시 70 이하로 되어 유기질 퇴비로서 규격이 미달되어 상품성도 없고 생산, 판매할 수 없기 때문에, 본 발명에서는 이러한 결점을 해결하기 위하여 창출한 것으로 상기 2차혼합물(5)에 유기물함량을 높이고 동시에 부숙도를 높이기 위하여 생석회(4)로 처리된 상기 2차혼합물(5) 100중량%에 대하여 완효성부산물원료(6) 30중량% 내지 50중량%를 혼합반응조(M)에 투입하여 상기 2차혼합물(5)과 함께 균일하게 혼합한 유기물인 3차혼합물(7)을 조성함으로서, 유기물을 추가 보충하고, 생석회(4) 투여로 인한 질소, 인산, 가리의 일부소멸을 방지하며, 또한 질소, 인산, 가리의 함유량을 높여주는 혼합안정화 공정을 거친 후, 상기 혼합반응조(M)내에서 3차혼합물(7)인 유기물의 부숙도를 높이기 위하여 적량의 수분공급과 산소공급을 계속 유지시킴으로서 2차 살균, 멸균 및, 부숙, 하는 공정을 거친 다음, 상기 3차혼합물(7)을 교반장(8)으로 배출하여 수분함량 40% ~ 50%로 건조시키는 공정을 거쳐서 본 발명인 유기질 퇴비를 제조하게 된다.The present invention is subjected to a selective grinding process of removing and pulverizing foreign substances (eg, plastics, vinyl paper, metals, etc.) from organic wastes composed of copper and vegetable residues, respectively, into the drying furnace, and the water content of the organic wastes (1). To 50% to 60%, and livestock manure (2) to adjust the water content of 60% to 70%, to adjust the water content of the livestock manure to 60% to 70% the manure (2) In order to prevent the loss of volatile components in the fertilizer components of the first, 70% by weight of the organic waste (1) and livestock manure (2) 30% by weight into the mixing reactor (M), the first mixture is uniformly mixed (3) after the second mixture was uniformly mixed by slowly administering 10% to 20% by weight of quicklime (4) to 100% by weight to the primary mixture (3) in the mixing reactor (M) ( 5) by forming a quicklime (4) on the surface of the secondary mixture (5) 2 When the temperature of the mixture (5) is about 100 degrees C to 120 degrees C, the process is stabilized by the first sterilization, sterilization, and decomposition of the fixed substance. In this case, the secondary mixture (5) has an organic content compared to the process standard. Significantly lower than 25%, the maturity is also 70 or less, because the organic compost is less than the standard, there is no commerciality and can not be produced, sold, the present invention was created to solve this drawback, the secondary mixture In order to increase the organic matter content in (5) and at the same time increase the maturity, 30 wt% to 50 wt% of the slow-acting by-product material (6) was added to 100 wt% of the secondary mixture (5) treated with quicklime (4). M) by adding to the secondary mixture (5) to form a third mixture (7), which is an organic material uniformly mixed with the organic material, by supplementing the organic matter, part of the nitrogen, phosphoric acid, girly due to the quicklime (4) administration Prevent extinction, After going through a stabilization process to increase the content of nitrogen, phosphoric acid and girly, the proper amount of water supply and oxygen supply are continuously maintained in order to increase the maturity of the organic material of the tertiary mixture (7) in the mixing reactor (M). After the second sterilization, sterilization, ripening, and the like process, the tertiary mixture (7) is discharged to the stirring station (8) to dry the water content 40% to 50% of the organic compost of the present invention To manufacture.

실시예
본 발명의 일실례를 예시하면, 동, 식물성 잔재물로 구성된 유기성폐기물(1)을 선별 분쇄하는 공정을 거쳐서 건조로내에 각각 투입하여, 상기 유기성폐기물(1)의 수분함량을 50% 내지 60%로 조절하여 상기 유기성폐기물(1) 700kg과, 축산분뇨(2)의 수분함량을 60% 내지 70%로 조절하여 덩어리가 지지 않게 (예컨대 계분덩어리등) 건조한 축산분뇨(2) 300kg을 상기 혼합반응조(M)에 투입하여, 1차혼합물(3)을 균일하게 혼합한 다음, 상기 혼합반응조(M)에 생석회(4) 100kg 내지 200kg을 1시간 정도 균일하게 혼합하여 2차혼합물(5)을 조성하여, 상기 2차혼합물(5)의 표면에 생석회(4)가 코팅되도록 하고, 이때 2차혼합물(5)은 산화소성반응을 일으키면서 약 15분 내지 20분이 경과되면, 상기 2차혼합물(5)에서 100도C 내지 120도C 의 발열이 되면서 1차 살균, 멸균을 하게 되고, 동시에 상기 유기성 폐기물중의 고형물질이 열 반응에 의하여 고형물질이 분해 되는 안정화공정을 거치게 되는데, 상기 1차혼합물(3) 투여하는 생석회(4)의 양은 계절에 따라 차이를 두게 되는바, 겨울철에는 200kg, 여름철에는 100kg, 봄,가을에는 150kg 내외의 생석회를 투여함으로서 2차혼합물에서 살균, 멸균과 고형물질이 쉽게 분해되는것을 수십회의 실험결과로 알게되었다.
이때 유기성폐기물(1)의 수분함량이 50% 이하이고, 축산분뇨(2)의 수분함량이 60% 이하일 경우에는 1차 혼합물(유기성폐기물 +가축분뇨)(3)에 생석회(4)를 투입하여 혼합할 때, 급격한 고열이 발생되어 열손실이 크게 되어 살균, 멸균 및 고형물질 분해의 효과가 저하되고, 반대로 유기성폐기물(1)의 수분함량이 60% 이상이고 가축분뇨(2)의 수분함량이 70% 이상일 경우에는, 1차 혼합물(3)에 생석회(4)를 투입하여 혼합할 때 급격한 고열은 발생되지 않으나, 2차혼합물(5)의 표면에 생석회(4)의 코팅률이 저하되고, 상품성도 저하되는 결점이 나타났고, 또한, 이때 2차혼합물(5)에서 산화소성반응시 100도C 내지 120도C 에 도달하는데, 20분 이상 지연되고, 또한 발열 시간은 연장되지만 2차혼합물(5)의 온도가 100도C 이하로 발열 되므로, 살균, 멸균 및 고형물질의 분해의 효과 저하되는 것을 장기간 시험결과 알게 되었다.
또한, 유기성폐기물(1)의 수분함량이 50% 이하이고, 축산분뇨(2)의 수분함량이 60% 이하일 경우 상기 2차혼합물(5)은 혼합반응조(M)내에서 유기성폐기물(1) 및 축산분뇨(2)와 생석회(4)가 산화소성 반응중 순간적인 고열로(즉 1차 혼합물이 생석회를 최초로 투여하는 순간부터) 유기물의 일부가 파괴되고, 또한 부숙도가 낮게 되는데 이 경우에는 일반퇴비와 가축퇴비의 공정규격보다 유기물함유량이 25% 이하가 되고, 부숙도는 70 이하로 되어 퇴비로서는 기준미달이 된다. 따라서 본 발명에서는 이러한 결점을 해결하기 위하여, 혼합반응조(M)내의 상기 2차혼합물(5) 1000kg에, 유기질 퇴비의 용도에 따라 완효성부산물원료(6) 300kg내지 500kg을 상기 혼합반응조(M)에 투입하고 균일하게 혼합하여, 3차혼합물(7)인 유기물을 조성하여, 질소, 인산, 가리등 유기물의 함유량을 높여주는 혼합안정화공정을 거친 다음 계절에 따라 10일 내지 15일간 부숙발효 공정을 지속하게 되는데, 이때 블로아로 산소를 지속적으로 공급하여 부숙발효를 효율적으로 시행하고, 혼합반응조(M)에서 발생하는 유기성폐기물(1)의 침출수를 따로 분리하여 투기처분하지 않고, 상기 유기성폐기물(1)의 침출수를 다시 혼합반응조(M)내에 1일 2~4회 분사하여, 부숙발효의 온도를 50도C 내지 90도C로 유지시켜서 2차 살균, 멸균 및 부숙공정을 거쳐서, 충분하게 부숙된 상기 3차혼합물(7)을 교반장(8)으로 배출하여 수분이 40% 내지 50%가 되도록 건조하는 공정을 거쳐서 본 발명인 유기질 퇴비를 친환경적으로 제조하게 된다.
Example
To illustrate an example of the present invention, the organic wastes (1) consisting of copper and vegetable residues are respectively introduced into a drying furnace through a process of selectively pulverizing, thereby adjusting the water content of the organic wastes (1) to 50% to 60%. The organic waste (1) 700kg and the livestock manure (2) to adjust the moisture content of 60% to 70% to prevent the lumps (for example, poultry mass, etc.) dry livestock manure (2) 300kg of the mixed reaction tank (M ), The primary mixture 3 is uniformly mixed, and then 100 kg to 200 kg of quicklime 4 is uniformly mixed in the mixing reactor M for about 1 hour to form a secondary mixture 5, The quicklime (4) is coated on the surface of the secondary mixture (5), wherein the secondary mixture (5) is about 15 minutes to 20 minutes while oxidizing the oxidative reaction, in the secondary mixture (5) First heat sterilization and sterilization while being heated to 100 degrees C to 120 degrees C The solid material in the organic waste is subjected to a stabilization process in which the solid material is decomposed by a thermal reaction. The amount of quicklime (4) administered in the primary mixture (3) is different depending on the season. The results of dozens of experiments showed that sterilization, sterilization and solid decomposition of secondary mixtures were easily carried out by administering quicklime of about 100kg in summer and 150kg in spring and autumn.
At this time, if the moisture content of the organic waste (1) is less than 50% and the moisture content of the livestock manure (2) is less than 60%, quicklime (4) is added to the primary mixture (organic waste + livestock manure) (3). When mixing, rapid high heat is generated and heat loss is increased, so that the effects of sterilization, sterilization and decomposition of solid materials are reduced. On the contrary, the water content of organic waste (1) is more than 60% and the water content of livestock manure (2). In the case of 70% or more, sudden high heat is not generated when the quicklime 4 is added to the primary mixture 3 and mixed, but the coating rate of the quicklime 4 on the surface of the secondary mixture 5 is lowered. The defect that the marketability is also lowered, and at this time, in the secondary mixture (5) when the oxidative reaction reaches 100 degrees C to 120 degrees C, a delay of 20 minutes or more, and the exothermic time is extended, but the secondary mixture ( 5) Because the temperature is generated below 100 ° C, sterilization, sterilization and decomposition of solid materials The long-term test result showed that it was degraded.
In addition, when the water content of the organic waste (1) is 50% or less, and the water content of the livestock waste (2) is 60% or less, the secondary mixture (5) is the organic waste (1) and in the mixed reaction tank (M) The livestock manure (2) and quicklime (4) are destroyed in an instantaneous high heat during the oxidative reaction (i.e. from the moment the primary mixture is first administered quicklime), which leads to the destruction of part of the organic matter and also low maturity. The organic matter content is 25% or less, and the maturity level is 70 or less than the compost and livestock compost standards, which is less than the standard. Therefore, in the present invention, in order to solve this drawback, in the mixing reaction tank (M) to 1000kg of the secondary mixture (5), 300kg to 500kg of the slow-acting by-product raw material (6) according to the use of organic compost (M) in the mixing reaction tank (M) The mixture is added and uniformly mixed to form an organic substance as a tertiary mixture (7), followed by a mixed stabilization process to increase the content of organic matter such as nitrogen, phosphoric acid, and galley, and then the fermentation fermentation process is continued for 10 to 15 days depending on the season. In this case, by continuously supplying oxygen to the blower to perform the fermentation fermentation efficiently, and separate the leachate of the organic waste (1) generated in the mixed reaction tank (M) separately without dumping the organic waste (1) Of leachate is again sprayed 2-4 times a day in the mixed reaction tank (M) to maintain the temperature of the fermentation fermentation at 50 ° C. to 90 ° C., followed by the second sterilization, sterilization, and lodging process, and the sufficiently mature phase By discharging the tertiary mixture 7 to the stirring station 8, the organic compost of the present invention is manufactured in an environmentally friendly manner through a process of drying the tertiary mixture 7 to 40% to 50% of moisture.

Claims (1)

유기성폐기물에서 이물질을 제거하고 분쇄하는 선별분쇄공정과 유기성폐기물에 생석회를 투여하여 상기 유기성폐기물의 표면에 생석회를 코팅하는 공정과 상기 유기성폐기물과 생석회의 혼합물을 건조하는 공정으로 구성된 유기질비료의 제조방법에 있어서, 동, 식물성 잔재물로 구성된 유기성폐기물에서 공지의 방법으로 이물질의 선별분쇄공정을 거친 상기 유기성폐기물의 수분함량을 50%~60%로, 가축분뇨의 수분함량은 60%~70% 되게 각각 건조로내에서 수분 조절한 상기 유기성폐기물 70중량%와 상기 축산분뇨 30중량%를 혼합반응조내에 투입하여 혼합한 1차혼합물을 조성한 다음 상기 1차혼합물 100중량%에 대하여 생석회 10중량%내지 20중량%를 서서히 투여하여 균일하게 혼합한 2차혼합물을 조성하여 약 20분 후에 상기 2차혼합물의 온도가 100도C ~ 120도C 정도에서 1차 살균, 멸균 및 고형물질의 분해로 안정화하는 공정과; 상기 2차혼합물의 유기물함량을 높힘과 동시에 부숙도를 높이기 위하여 상기 2차혼합물 100중량 %에 대하여 완효성부산물원료 30중량%내지 50중량%를 상기 혼합반응조내에서 균일하게 혼합하여 3차혼합물을 조성하여 유기물을 추가보충하고 동시에 부숙도를 높이는 혼합안정화 및 살균, 멸균, 부숙공정과; 상기 3차혼합물을 교반장으로 배출하여 건조하는 것을 특징으로 하는 유기질퇴비의 제조방법A method for producing organic fertilizer comprising a screening process for removing and grinding foreign matters from organic wastes and coating quicklime on the surface of organic wastes by administering quicklime to organic wastes and drying the mixture of organic wastes and quicklime In the organic waste consisting of copper and vegetable residues, the water content of the organic waste, which has been subjected to the screening and crushing process of foreign substances by a known method, is 50% to 60%, and the water content of livestock manure is 60% to 70%, respectively. 70% by weight of the organic waste adjusted in the drying furnace and 30% by weight of livestock wastes were added to a mixing reactor to form a mixed primary mixture, and then 10% by weight to 20% by weight of quicklime based on 100% by weight of the primary mixture. After slowly administering to form a homogeneously mixed secondary mixture after about 20 minutes the temperature of the secondary mixture is 100 ° C ~ 120 ° C Stabilizing by primary sterilization, sterilization and decomposition of the solid material in the degree; In order to increase the organic matter content of the secondary mixture and at the same time increase the maturity, a tertiary mixture is formed by uniformly mixing 30 wt% to 50 wt% of the raw by-product by-product with respect to 100 wt% of the secondary mixture. Mixing and stabilizing and sterilizing, sterilizing, and supplementing the organic material to further supplement and at the same time increase the maturity; Method for producing an organic compost, characterized in that the tertiary mixture is discharged to the stirring station and dried
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