KR20110042909A - Fermentation Method and Fermentation System of Organics - Google Patents

Fermentation Method and Fermentation System of Organics Download PDF

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KR20110042909A
KR20110042909A KR1020090099779A KR20090099779A KR20110042909A KR 20110042909 A KR20110042909 A KR 20110042909A KR 1020090099779 A KR1020090099779 A KR 1020090099779A KR 20090099779 A KR20090099779 A KR 20090099779A KR 20110042909 A KR20110042909 A KR 20110042909A
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fermentation
tank
discharge port
organic
organic matter
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KR101075274B1 (en
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최인숙
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    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/40—Treatment of liquids or slurries
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00—Other organic fertilisers
    • C05F11/08—Organic fertilisers containing added bacterial cultures, mycelia or the like
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/60—Heating or cooling during the treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F5/00—Fertilisers from distillery wastes, molasses, vinasses, sugar plant or similar wastes or residues, e.g. from waste originating from industrial processing of raw material of agricultural origin or derived products thereof
    • C05F5/002—Solid waste from mechanical processing of material, e.g. seed coats, olive pits, almond shells, fruit residue, rice hulls
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F9/00—Fertilisers from household or town refuse
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F9/00—Fertilisers from household or town refuse
    • C05F9/02—Apparatus for the manufacture
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05G—MIXTURES 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
    • C05G5/00—Fertilisers characterised by their form
    • C05G5/20—Liquid fertilisers
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Pest Control & Pesticides (AREA)
  • Mechanical Engineering (AREA)
  • Botany (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE: A method and an apparatus for processing the fermentation of organic materials are provided to convert organic wastes into liquefied fertilizer by implementing multi-stepped fermenting processes. CONSTITUTION: An apparatus for processing the fermentation of organic materials includes a storing bath(1), a stabilizing bath(2), a discharging material transferring unit(3), a fermenting bath(4), a high temperature supplying unit(5), and a liquefied fertilizer aging bath(6). Organic materials are stored in the storing bath and are primarily pulverized. The pulverized organic materials are transferred to the stabilizing bath and are secondarily pulverized. A sterilization process is processed using air with high temperature more than 70 degrees Celsius. A fermenting agent and strain are introduced into the organic materials to discharge stabilized and aged organic materials. The organic materials are fermented and aged.

Description

유기물의 발효처리방법 및 발효처리장치 { A METHOD OF PROCESSING FERMENTATION OF ORGANIC MATERIAL AND METHOD OF PROCESSING FERMENTATION DEVICE }Fermentation Method and Fermentation System of Organic Matter {A METHOD OF PROCESSING FERMENTATION OF ORGANIC MATERIAL AND METHOD OF PROCESSING FERMENTATION DEVICE}

본 발명은 유기물의 발효처리방법 및 발효처리장치에 관한 것으로, 더욱 구체적으로 설명하면, 골프장의 깍여진 잔디의 처리나 음식물 쓰레기와 같은 유기물을 저장조, 안정조, 발효조, 액비숙성조를 통한 다단계의 발효처리를 통하여 폐기처리가 어려운 폐기물에 가까운 유기물을 유용한 자원인 액상 비료로 변환시키는 것이 가능한 유기물의 발효처리방법 및 발효처리장치에 관한 것이다. The present invention relates to a fermentation treatment method and a fermentation treatment apparatus for organic matters, and more specifically, a multi-stage through a storage tank, a stabilizer tank, a fermentation tank, and a liquid maturation tank for organic matters such as treatment of mowed grass or food waste in a golf course. The present invention relates to a fermentation method and a fermentation treatment apparatus for an organic material capable of converting an organic material close to a waste which is difficult to be disposed of through fermentation into a liquid fertilizer which is a useful resource.

일반적으로, 넓은 공간에 잔디가 자라는 골프장에서는 주기적으로 잔디를 깍아 주어 절단상태의 예초된 잔디가 다량으로 발생되게 된다. 이와 같이 발생된 예초된 잔디는 골프장에서 많은 농약을 살포하여 자라게 되므로 가축의 사료로 사용될 수 없어서 부득이하게 폐기물로서 버려지고 있으나, 골프장의 넓이가 수십만평으로 너무나 넓으므로 예초된 잔디의 발생량이 많게 되어 폐기물로서 처리하기에는 어려움이 많아 그 처리에 많은 곤란이 발생되고 있는 실정이다. 이후의 설명에서는 '유기물'이 예초된 잔디를 포함한다.Generally, in a golf course where grass grows in a large space, the grass is periodically mowed to generate a large amount of mowed grass in a cut state. The mowed grass generated in this way is grown by spraying a lot of pesticides on the golf course, so it cannot be used as feed for livestock, but it is inevitably thrown away as waste. There are many difficulties in treating as waste and many difficulties arise in the treatment thereof. In the following description, 'organic' includes grass that has been mowed.

또한, 음식물 쓰레기와 같은 사료로서 사용가능한 유기물도 내부에 염분에 포함되어 있어 사료로 처리되지 못하고 폐기물로서 해양투기와 같은 처리가 이루어지고 있는 실정이나, 이러한 해양투기는 조만간에 금지되어 음식물 쓰레기의 처리에 많은 노력과 연구가 행해지고 있는 실정이다.In addition, organic matter that can be used as feed, such as food waste, is also contained in the salt, which is not treated as feed, but is treated as waste, such as ocean dumping, but such dumping is prohibited soon, so the disposal of food waste A lot of effort and research is being done.

이러한 예초된 잔디나 음식물 쓰레기(이하 '유기물'이라 칭함)를 처리하기 위한 처리장치는 대부분이 발효처리과정이 수행되지 않고 단지, 감량이나 건조 및 소멸의 단순처리만을 수행하는 것이 대부분으로서 이러한 장치에서의 처리후에 유기물이 발효가 되어 악취가 발생되거나 오염물이 발생되어 그 처리가 어려워지게 되는 문제점이 있었다.Most of the treatment apparatus for treating such mowed grass or food waste (hereinafter referred to as 'organic matter') is not performed fermentation process, but only the simple treatment of weight loss, drying and extinction is performed in such an apparatus. After the treatment of the organic matter is fermented to produce a bad smell or contaminants there was a problem that the treatment becomes difficult.

본 발명의 목적은, 이러한 문제점을 해결하기 위한 것으로, 처리가 어려운 유기물을 저장조, 안정조, 발효조, 액비숙성조로 연이어 거치면서 발효되게 하므로서 처리가 곤란한 유기 폐기물을 유용한 자원인 액상비료로 변환시키는 것이 가능하게 되어 폐기물의 처리가 용이하게 되면서도 자원으로 다시 활용하는 것이 가능하게 하는 유기물의 발효처리방법 및 발효처리장치를 제공하는 것이다. An object of the present invention is to solve such a problem, and to convert the organic waste, which is difficult to process, into a liquid fertilizer, which is a difficult resource, by making it difficult to process the organic matter which is difficult to process into a storage tank, a stabilization tank, a fermentation tank, and a liquid aging tank. It is possible to provide a fermentation treatment method and a fermentation treatment apparatus for an organic material, which makes it possible to easily treat waste and reuse it as a resource.

본 발명의 이러한 목적은, 유기물을 일단은 저장조에 저장하여 모래와 같은 침전물을 발생시키며 1차로 분쇄시키는 저장단계와, 이와 같이 1차로 분쇄되고 침전물처리가 수행된 예초된 잔디와 같은 유기물을 경사 스크류밸트를 통하여 안정조로 이송시켜 교반날개를 통하여 분쇄시켜 2차적인 처리를 수행하고 70℃ 이상의 고온공기를 가하여 멸균과 무균화를 시키고 발효촉매제와 균주를 투입하여 안정화시키면서 안정화되고 숙성된 유기물을 토출시키는 안정화단계와, 이와 같이 토출된 유기물이 저장버켓을 통하여 이송시키는 이송단계와, 상기 저장버켓에 의하여 유입되고 동시에 열풍가열장치에 의하여 고온으로 가열된 가열공기를 혼입시켜 토출된 유기물을 발효시키는 발효단계와, 상기 발효단계를 통하여 발효된 유기물을 진공펌프로 인출하여 액비숙성조로 이송시켜 숙성시키는 숙성단계를 포함하는 본 발명에 따른 유기물의 발효처리방법에 의하여 달성된다.This object of the present invention, the storage step of storing the organic matter once in a reservoir to generate a precipitate, such as sand, and crushed first, and decanted screw organic matter, such as mowed grass that was primarily crushed and sedimentation treatment Transfer to a stable tank through the belt to grind through the stirring blade to perform secondary treatment, sterilization and sterilization by adding high temperature air of 70 ℃ or more and discharge the stabilized and matured organic material while stabilizing by adding fermentation catalyst and strain A stabilization step, a transfer step of transferring the discharged organic material through the storage bucket, and a fermentation step of fermenting the discharged organic material by mixing heated air introduced by the storage bucket and heated at a high temperature by a hot air heater. And, withdraw the organic material fermented through the fermentation step with a vacuum pump It is achieved by the fermentation treatment method of an organic material according to the present invention comprising a aging step to transfer to the liquid aging tank to age.

본 발명의 이러한 목적은, 분쇄기가 내부에 회전가능하게 설치되며 하부에는 상방으로 연장되는 이송컨베어의 일단부가 설치되고 저면에는 침전물배출구가 설치된 저장조와, 상기 저장조의 이송컨베어가 타단부가 상부에 설치되며 내부에는 분쇄기가 회전가능하게 설치되며 하부에는 침전물이 배출되는 배출구가 설치되며 상부의 중간에는 안정화된 유기물이 배출되는 토출구가 형성되고 하부에는 급기블로어와 히터가 설치되어 고온공기가 공급되는 안정조와, 상기 안정조에서 토출된 유기물이 저장되는 저장버켓을 승하강되게 이송시키며 저장버켓내의 유기물을 발효조로 운반시키는 운반기가 설치된 토출물운반구와, 상기 토출물운반구의 저장버켓내의 유기물이 유입되는 유입구가 설치되고 내부에는 교반기가 회전가능하게 설치되고 유기물을 발효가 가능하도록 고온공기가 공급되는 발효조와, 상기 발효조내에 고온공기를 공급하는 고온공급기와, 상기 발효조내의 발효물이 이송되어 상기 발효물을 숙성시키는 액비숙성조를 포함하는 본 발명에 따른 유기물의 발효처리장치에 의하여 달성된다.This object of the present invention, the grinder is rotatably installed in the interior and one end of the conveying conveyor extending upwards is installed on the bottom and the bottom of the reservoir is installed with a discharge outlet, the transfer conveyor of the reservoir is installed on the other end In the inside, the grinder is rotatably installed, and the lower part is provided with an outlet for discharging sediment. In the middle of the upper part, an outlet for discharging stabilized organic material is formed, and the lower part is provided with an air supply blower and a heater to supply hot air. A discharge conveyance port having a transporter for transporting the storage bucket storing the organic matter discharged from the stabilization tank to move up and down and transporting the organic matter in the storage bucket to the fermentation tank, and an inlet through which the organic matter in the storage bucket of the discharge transport port is introduced. Inside the stirrer and rotatable The organic substance according to the present invention includes a fermentation tank to which high temperature air is supplied to enable fermentation, a high temperature supply supplying high temperature air into the fermentation tank, and a liquid non-aging tank to transfer fermentation products in the fermentation tank to mature the fermentation product. Achieved by a fermentation treatment apparatus.

본 발명에 따른 유기물의 발효처리방법 및 발효처리장치는 처리가 곤란한 유기 폐기물을 1차로 저장하여 분쇄시키는 저장조와, 안정화시키는 안정조와, 발효시키는 발효조와, 숙성시키는 숙성조를 거치게 하여 유용한 자원인 액상비료로 변환시키는 것이 가능하여 폐기물인 유기물을 액상비료로 재활용하게 된다는 우수한 효과가 있다.Fermentation treatment method and fermentation apparatus for organic matter according to the present invention is a liquid that is a useful resource through a storage tank for storing and pulverizing organic waste difficult to process first, a stabilizing tank for stabilization, a fermentation tank for fermentation, and a aging tank for aging. It is possible to convert to fertilizers has an excellent effect of recycling the organic matter as a liquid fertilizer.

본 발명의 제1실시예에 따른 유기물의 발효처리방법은, 도 1에 도시된 바와 같이, 유기물을 일단은 저장조에 저장하여 모래와 같은 침전물을 발생시키며 1차로 분쇄시키는 저장단계와, 이와 같이 1차로 분쇄되고 침전물처리가 수행된 예초된 잔디와 같은 유기물을 경사 스크류밸트를 통하여 안정조로 이송시켜 교반날개를 통하여 분쇄시켜 2차적인 처리를 수행하고 70℃ 이상의 고온공기를 가하여 멸균과 무균화를 시키고 발효촉매제와 균주를 투입하여 안정화시키면서 안정화되고 숙성된 유기물의 토출물을 토출시키는 안정화단계와, 이와 같이 토출된 토출물이 저장버켓을 통하여 이송시키는 이송단계와, 상기 저장버켓에 의하여 유입되고 동시에 열풍가열장치에 의하여 고온으로 가열된 가열공기를 혼입시켜 토출물을 발효시키는 발효단계와, 상기 발효단계를 통하여 발효된 발효물을 진공펌프로 인출하여 액비숙성조로 이송시켜 숙성시키는 숙성단계를 포함한다.The fermentation treatment method of the organic material according to the first embodiment of the present invention, as shown in Figure 1, storing the organic matter once in a storage tank to generate a precipitate, such as sand, the first storage step, and thus 1 Organic matters such as mowed grass, which was pulverized and sedimented by car, were transferred to a stable tank through an inclined screw belt, pulverized through agitating blades, and subjected to secondary treatment, and sterilized and sterilized by applying hot air of 70 ° C. or higher. Stabilization step of discharging the discharge of the stabilized and matured organic material while stabilizing by adding a fermentation catalyst and strain, a transfer step of transferring the discharged discharged through the storage bucket, and the hot air introduced at the same time by the storage bucket A fermentation step of fermenting a discharged product by mixing heated air heated to a high temperature by a heating device; The fermentation product is fermented through a fermentation step is taken out with a vacuum pump transfer to a liquid aging tank and the aging step of aging.

본 발명의 제1실시예에 따른 유기물의 발효처리장치(A)는, 도 2에 도시된 바와 같이, 분쇄기(11)가 내부에 회전가능하게 설치되며 하부에는 이송컨베어(12)가 설치된 저장조(1)와, 상기 저장조(1)의 이송컨베어(12)가 상부에 설치되며 내부에는 분쇄기(21)가 회전가능하게 설치되며 하부에는 침전물이 배출되는 배출구(22)가 설치되며 상부의 중간에는 유기물의 토출물이 배출되는 토출구(23)가 형성된 안정조(2)와, 상기 안정조(2)에서 토출된 유기물의 토출물이 저장되는 저장버켓(31)을 상방으로 이송시키는 운반기(32)가 설치된 토출물운반구(3)와, 상기 토출물운반구(3)의 저장버켓(31)내의 토출물이 유입되는 유입구(41)가 설치되고 내부에는 교반기(42)가 회전가능하게 설치된 발효조(4)와, 상기 발효조(4)내에 고온공기를 공급하는 고온공급기(5)와, 상기 발효조(4)내의 발효물이 이송되어 상기 발효물을 숙 성시키는 액비숙성조(6)를 포함한다.In the fermentation treatment apparatus (A) of the organic material according to the first embodiment of the present invention, as illustrated in FIG. 2, a grinder 11 is rotatably installed therein and a storage tank in which a conveying conveyor 12 is installed at a lower portion thereof. 1), and the conveying conveyor 12 of the reservoir 1 is installed on the upper side, and the grinder 21 is rotatably installed therein, and an outlet 22 for discharging sediment is installed in the lower part, and the organic material in the middle of the upper part. A stabilizer tank 2 having a discharge port 23 through which discharges of the discharges are discharged is formed, and a carrier 32 for transferring upwardly a storage bucket 31 in which discharges of organic substances discharged from the stabilizer tank are stored. The fermentation tank 4 in which the discharge port carrying port 3 is provided, and the inlet port 41 through which the discharge in the storage bucket 31 of the discharge port carrying port flows in. The stirrer 42 is rotatably installed therein. And a high temperature feeder (5) for supplying hot air into the fermentation tank (4), and the fermentation tank (4). The fermentation product in the transfer comprises a liquid maturation tank (6) for aging the fermentation product.

상기 저장조(1)는 내부에 분쇄기(11)가 회전가능하게 설치되어 유입된 예초되어 절단된 잔디인 유기물을 원하는 크기로 분쇄하는 과정을 거치면서 유기물인 잔디에 묻은 흙과 같은 불순물을 잔디에서 털어내어 하부에는 고운 모래와 같은 침전물이 발생되고 이와 같은 침전물은 하부의 침전물배출구(13)를 통하여 배출되고, 분쇄된 잔디인 유기물은 이송컨베어(12)를 타고 안정조(2)로 이송되게 된다.The reservoir 1 is rotatably installed inside the grinder 11, the process of crushing the organic matter, which is the mowed cut grass introduced into the desired size while shaking the impurities, such as soil in the grass of the organic matter from the grass Sediment such as fine sand is generated in the lower portion, and the precipitate is discharged through the sediment discharge port 13 in the lower portion, and the organic matter, which is crushed grass, is transferred to the stabilization tank 2 by the transfer conveyor 12.

상기 안정조(2)는 저장조(1)의 이송컨베어(12)로 이송된 1차로 파쇄된 잔디인 유기물이 2차로 분쇄기(21)를 통하여 분쇄되고 안정조에서 3~4일간 안정되면서 숙성된다. 상기 안정조(2)는 원통형으로 형성되고 상부에는 맨홀(24)이 형성되고 하부에는 공기를 불어 넣는 하부 블로어(25)가 설치되고, 하부에는 침전물이 배출되는 배출구(22)가 설치되어 있다. 상기 분쇄기(21)는 페들형으로 구동축(211)에 6개의 페들(212)이 종방향으로 설치되어 유기물을 5mm내외의 고른 입자로 분쇄시킨다. 상기 블로어(25)의 상부에는 히터(26)가 설치되어 안정조(2)내로 공급되는 공기를 약 80℃로 가열하여 안정조(2)내부로 공급하므로서 안정조(2)내부의 각종 병원균을 멸균 또는 무균화시킨다.The stabilization tank 2 is aged while being organically crushed through the grinder 21 in the first crushed grass transferred to the conveying conveyor 12 of the storage tank 1 and stabilized in the stabilization tank for 3 to 4 days. The stabilizer 2 is formed in a cylindrical shape, a manhole 24 is formed in the upper portion, a lower blower 25 for blowing air is installed in the lower portion, and a discharge port 22 through which a precipitate is discharged is installed in the lower portion. The grinder 21 has a paddle shape, in which six paddles 212 are installed in the drive shaft 211 in the longitudinal direction to grind organic matter into even particles of about 5 mm. The heater 26 is installed at the upper part of the blower 25 and heats the air supplied into the stabilizer 2 to about 80 ° C. to supply the inside of the stabilizer 2 to supply various pathogens inside the stabilizer 2. Sterilize or sterilize.

상기 분쇄기(21)는 유기물을 잘 뒤집을 수 있도록 25~30rpm의 속도로 회전된다. 이와 같이 3~4일간 숙성된 유기물은 상부의 토출구(23)를 통하여 저장버켓(31)으로 배출된다.The grinder 21 is rotated at a speed of 25 ~ 30rpm so as to overturn the organic matter well. Thus, the organic material aged for 3 to 4 days is discharged to the storage bucket 31 through the upper discharge port 23.

본 실시예에서 50톤 용량의 안정조(2)를 기준으로, 상기 안정조(2)의 맨홀(24)을 통하여 처음에 15kg의 발효촉매제와 0.3%의 균주를 투입하고 다음회부터 는 월10kg의 발효촉매제와 0.15%의 균주를 보충시킨다.In the present embodiment, based on a 50 ton capacity stabilizer (2), 15 kg of fermentation catalyst and 0.3% of strain are initially introduced through the manhole (24) of the stabilizer (2), and the next time 10 kg per month. The fermentation catalyst of and 0.15% of the strain is supplemented.

상기 토출물운반구(3)는 토출구(23)의 하방에 배치되어 유기물이 수납되는 저장버켓(31)과, 상기 저장버켓(31)을 상방으로 이송시키는 운반기(32)를 포함한다. 상기 저장버켓(31)은 상부가 개방된 육면체로 형성되며 상기 운반기(32)의 지지받침대(321)상에 배치되고, 상기 운반기(32)의 지지받침대(321)가 승강이동되어 상기 발효조(4)로 유기물을 공급한다. 상기 운반기(32)는 지지받침대(321)를 승강시키는 구동장치가 설치되어 있으나 이에 대한 구체적인 설명은 생략한다. 운반기(32)의 상부로 상승된 저장버켓(31)이 기울어지면서 발효조(4)의 유입구(41)를 통하여 발효조(4)내로 유입된다.The discharge transport port 3 includes a storage bucket 31 disposed below the discharge port 23, in which organic matter is stored, and a carrier 32 for transferring the storage bucket 31 upward. The storage bucket 31 is formed of a hexahedron with an open top and is disposed on the support base 321 of the carrier 32, and the support base 321 of the carrier 32 is moved up and down to the fermentation tank 4. Feed organic matter). The carrier 32 is provided with a driving device for lifting the support base 321, but a detailed description thereof will be omitted. The storage bucket 31 which is raised to the upper portion of the carrier 32 is inclined and introduced into the fermentation tank 4 through the inlet 41 of the fermentation tank 4.

상기 발효조(4)는 상기 안정조(2)와는 완전히 차별화된 발효기능을 갖고 있으며 상기 안정조(2)와는 별도로 설치되어 독자적으로 구동된다. 상기 안정조(2)는 발효를 쉽게 하기 위한 조건을 충족시키고 발효조(4)는 상기 안정조(2)에 의하여 안정화된 유기물을 발효를 시키는 것이다.  The fermentation tank (4) has a fermentation function that is completely different from the stabilizer (2) and is installed separately from the stabilizer (2) to be driven independently. The stabilizer (2) meets the conditions for easy fermentation and the fermentation tank (4) is to ferment the organic material stabilized by the stabilizer (2).

상기 발효조(4)는, 원통형 몸체(40)와, 상기 원통형 몸체(40)의 내부에는 교반기(42)가 설치되어 있다. 상기 교반기(42)는 리본형 타입이고, 구동축(421)을 통하여 5rpm ~ 30rpm의 저속으로 회전되면서 발효수행의 최적의 온도 및 산소조건을 조성케 한다. 상기 발효조(4)는 생물학적 처리의 호기성 발효조건이기 때문에 충분한 산소공급이 필수조건이므로 발효대상물 중량의 약 12중량%의 공기공급을 후술되는 고온공기공급기(5)를 통하여 유지시킨다. 상기 발효조(4)의 상부에는 맨홀(43)이 설치되어 발효촉매제인 발효제와 발효대상물 중량의 0.2중량%인 균주를 혼합투 입할 수 있게 되어 있다. 상기 발효조(4)의 상부에는 열교환기(44)가 설치되어 있다. 상기 열교환기(44)는 브로와를 통하여 공급되는 산소의 온도를 상승 또는 하강시키는 기능을 수행한다. 상기 발효조(4)의 상부의 측면에는 가스가 배출되는 가스배출구(45)가 설치되고 상기 가스배출구(45)를 통하여 배출가스가 배출되고 선단의 탈취부(46)를 통하여 배출가스가 탈취된다. 발효처리과정에서 자체발열과 간접발열에 의해 증발되는 다량의 기체와 소량의 유해가스를 동시에 처리할 수 있도록 탈취장치 및 열교환기를 설치하여 산화처리되게 하였다. 상기 발효조(4)의 내부의 온도는 55도씨 ~ 65도씨로 유지되어 발효에 최적의 온도를 유지한다.The fermentation tank 4 is provided with a cylindrical body 40 and an agitator 42 inside the cylindrical body 40. The stirrer 42 is a ribbon type, and rotates at a low speed of 5rpm ~ 30rpm through the drive shaft 421 to create the optimum temperature and oxygen conditions of fermentation. Since the fermentation tank 4 is an aerobic fermentation condition of biological treatment, sufficient oxygen supply is a necessary condition, so that an air supply of about 12% by weight of the weight of the fermentation object is maintained through the hot air supply 5 described later. The upper part of the fermentation tank (4) is provided with a manhole (43) is able to mix-in the strain of 0.2% by weight of the fermentation agent and the fermentation target weight of the fermentation catalyst. The heat exchanger 44 is installed in the upper part of the fermentation tank 4. The heat exchanger 44 performs a function of raising or lowering the temperature of the oxygen supplied through the brower. The gas discharge port 45 is installed at the side of the upper portion of the fermentation tank 4, the discharge gas is discharged through the gas discharge port 45 and the discharge gas is deodorized through the deodorizing portion 46 of the tip. During the fermentation process, a deodorizer and a heat exchanger were installed and oxidized so that a large amount of gas and a small amount of harmful gas evaporated by self-heating and indirect heat-heating could be simultaneously processed. The temperature inside the fermentation tank 4 is maintained at 55 ° C ~ 65 ° C to maintain the optimum temperature for fermentation.

상기 고온공급기(5)는 상기 발효조(4)내에 발효최적온도로 고온의 공기를 공급하는 장치로서, 하부에 급기블로워(51)가 설치되고 상부에 공기가열기(52)가 설치되어 있다. 상기 공기가열기(52)의 배출부상에는 온도감지센서(53)가 설치되어 있어, 급기블로워(51)를 통하여 송풍된 공기는 공기가열기(52)에서 고온으로 가열되고 온도감지센서(53)는 정해진 온도를 초과되면 이를 감지하여 공기가열기(52)를 오프 작동을 시키고, 정해진 온도의 이하로 되면 공기가열기(52)를 온 작동시키면서 발효조(4)내로 송풍되는 공기의 온도를 일정하게 제어하게 되는 구조이다. 본 실시예에서, 상기 공기가열기(52)에서 가열되는 공기의 온도는 약 55℃이고, 이와 같이 가열된 공기는 발효조(4)내로 유입되어 발효를 수행하는 최적의 조건을 제공한다. The hot feeder (5) is a device for supplying high temperature air at the fermentation optimum temperature in the fermentation tank (4), an air supply blower (51) is installed at the lower part and an air heater (52) is installed at the upper part. The temperature sensor 53 is installed on the discharge part of the air heater 52, so that the air blown through the air supply blower 51 is heated to a high temperature in the air heater 52 and the temperature sensor 53 Detects this when the predetermined temperature is exceeded to turn off the air heater 52, and when the temperature is lower than the predetermined temperature, the air heater 52 is turned on and the temperature of the air blown into the fermentation tank 4 is kept constant. It is a structure to be controlled. In this embodiment, the temperature of the air heated in the air heater 52 is about 55 ℃, the heated air is introduced into the fermentation tank (4) to provide the optimum conditions for performing the fermentation.

상기 액비숙성조(6)는 바닥과 측면에 열선이 깔린 숙성조몸체(60)에 의하여 원하는 온도를 유지할 수 있게 되어 액비숙성조(6)의 내부온도를 일정하게 조절할 수 있으며, 상기 액비숙성조(6)는 발효조에서 100% 발효되지 않은 부분을 액상비료로 100% 숙성시킨다. 상기 액비숙성조(6)의 상부에는 상기 발효조(4)에서 연결되어 유기물이 공급되는 공급관(61)이 설치되고, 액비숙성조(6)의 내부에는 수중믹서기(62)가 설치되고, 측면에는 토출구(63)가 형성되어 있다. 상기 액비숙성조(6)는 유기물이 숙성되기 적당한 온도인 23~45℃로 1~3일동안 유지되고 이와 같이 숙성된 액비는 토출구(63)를 통하여 토출되어 액비로 사용할 수 있게 되는 것이다.The liquid aging tank (6) is able to maintain the desired temperature by the aging tank body 60, the heating wire is laid on the bottom and side, it is possible to constantly adjust the internal temperature of the liquid aging tank (6), the liquid aging tank (6) ferment the 100% fermented portion of the fermenter 100% with liquid fertilizer. The upper part of the liquid aging tank (6) is connected to the fermentation tank (4) is provided with a supply pipe 61 for supplying organic matter, the inside of the liquid aging tank (6) is installed an underwater mixer (62), on the side The discharge port 63 is formed. The liquid aging tank (6) is maintained for 1 to 3 days at 23 ~ 45 ℃, which is a suitable temperature for the organic material is aged is to be discharged through the discharge port 63 to be used as a liquid ratio.

이와 같은 구성을 갖는 본 발명에 따른 유기물의 발효처리장치(A)의 작동을 설명하면, 유기물이 저장조(1)내로 투입되어 분쇄기(11)에 의하여 1차로 분쇄되고, 유기물내에 포함된 모래와 같은 침전물은 저장조(1)의 하부의 침전물배출구(13)를 통하여 배출되고, 분쇄된 잔디인 유기물은 이송컨베어(12)를 타고 안정조(2)로 이송되게 된다. 이와 같이 이송된 1차로 파쇄된 잔디인 유기물이 2차로 분쇄기(21)를 통하여 분쇄되고 안정조(2)에서 1~3일간 안정되면서 숙성되고, 숙성된 유기물은 상부의 토출구(23)를 통하여 저장버켓(31)으로 배출된다. 숙성된 유기물이 저장된 저장버켓(31)은 상기 운반기(32)의 지지받침대(321)상에 배치되어 상승이동되어 상기 발효조(4)의 유입구(41)를 통하여 발효조(4)내로 유기물을 공급한다. 이와 같이 발효조(4)내로 공급되어 충진된 유기물은 상기 발효조(4)내에 고온공기를 공급하는 고온공급기(5)에서 55℃로 가열되어 발효조(4)내에 공급되어 최적의 발효조건을 이루게 하고, 발효조(4)에서 1~3일간 발효되고, 이와 같이 발효된 유기물은 발효조(4)에서 연결되어 유기물이 공급되는 공급관(61)을 통하여 액비숙성조(6)로 공급되고, 이와 같이 액비숙성조(6)로 공급된 유기물은 숙성되기 적당한 온도인 30℃의 내외의 온도로 1~3일동안 유지되고 이와 같이 숙성된 액비는 토출구(63)를 통하여 토출되어 액비로 사용할 수 있게 되는 것이다.Referring to the operation of the organic matter fermentation treatment apparatus (A) according to the present invention having such a configuration, the organic matter is introduced into the storage tank (1) and pulverized primarily by the crusher 11, such as sand contained in the organic matter The sediment is discharged through the sediment discharge port 13 in the lower part of the storage tank 1, the organic matter which is crushed grass is transported to the stabilization tank (2) by the transfer conveyor (12). The organic matter, which is the first crushed grass transferred in this way, is crushed through the crusher 21 and aged for 1 to 3 days in the stabilization tank 2, and the aged organic matter is stored through the upper discharge port 23. It is discharged to the bucket (31). The storage bucket 31 in which the aged organic matter is stored is disposed on the support base 321 of the carrier 32 and moved upward to supply the organic matter into the fermentation tank 4 through the inlet 41 of the fermentation tank 4. . As such, the organic material supplied and filled into the fermentation tank 4 is heated to 55 ° C. in a high temperature feeder 5 for supplying high temperature air into the fermentation tank 4, and supplied to the fermentation tank 4 to achieve optimum fermentation conditions. The fermentation tank 4 is fermented for 1 to 3 days, the fermented organic material is supplied to the liquid aging tank 6 through the supply pipe 61 which is connected to the fermentation tank 4 and is supplied with the organic material, and thus the liquid aging tank. The organic material supplied to (6) is maintained at a temperature of about 30 ° C., which is a temperature suitable for aging, for 1 to 3 days, and the liquid ratio thus aged is discharged through the discharge port 63 to be used as the liquid ratio.

본 발명에 따른 유기물의 발효처리방법 및 발효처리장치는 일반 발효처리장치의 제조공장이나 발효처리를 사용하는 작업장에서 반복적으로 사용하는 것이 가능하다고 할 것이므로 산업상 이용가능성이 있는 발명이라고 할 것이다.The fermentation treatment method and the fermentation treatment apparatus of the organic material according to the present invention will be said to be an industrially applicable invention because it can be repeatedly used in a manufacturing plant of a general fermentation treatment apparatus or a workplace using a fermentation treatment.

도 1은 본 발명의 제1실시예에 따른 유기물 발효처리방법의 공정도1 is a process chart of the organic fermentation treatment method according to a first embodiment of the present invention

도 2는 본 발명의 제1실시예에 따른 유기물 발효처리장치의 개략적인 평면도2 is a schematic plan view of an organic fermentation treatment apparatus according to a first embodiment of the present invention.

도 3은 본 발명의 제1실시예에 따른 유기물 발효처리장치의 개략적인 정면도3 is a schematic front view of an organic fermentation treatment apparatus according to a first embodiment of the present invention.

*도면의 주요 부분에 대한 부호의 설명** Description of the symbols for the main parts of the drawings *

1. 저장조 2. 안정조 3. 토출물운반구1. Storage tank 2. Stable tank 3. Discharge container

4. 발효조 5. 고온공급기 6. 액비숙성조4. Fermentation tank 5. Hot feeder 6. Liquid maturation tank

Claims (2)

유기물의 발효처리방법에 있어서,In the fermentation treatment method of organic matter, 상기 유기물의 발효처리방법은, 유기물을 일단은 저장조에 저장하여 모래와 같은 침전물을 발생시키며 1차로 분쇄시키는 저장단계와, The fermentation treatment method of the organic material, the storage step of first storing the organic matter in a storage tank to generate a precipitate, such as sand and pulverized first, 이와 같이 1차로 분쇄되고 침전물처리가 수행된 예초된 잔디와 같은 유기물을 경사 스크류밸트를 통하여 안정조로 이송시켜 교반날개를 통하여 분쇄시켜 2차적인 처리를 수행하고 70℃ 이상의 고온공기를 가하여 멸균과 무균화를 시키고 발효촉매제와 균주를 투입하여 안정화시키면서 안정화되고 숙성된 유기물의 토출물을 토출시키는 안정화단계와, As such, organic matters such as mowed grass, which are first ground and subjected to sedimentation treatment, are transferred to a stable tank through an inclined screw belt, pulverized through agitating blades, and subjected to secondary treatment. A stabilization step of discharging the discharge of the stabilized and matured organic matter while stabilizing and adding a fermentation catalyst and a strain; 이와 같이 토출된 유기물이 저장버켓을 통하여 이송시키는 이송단계와, A transfer step of transferring the discharged organic matter through the storage bucket; 상기 저장버켓에 의하여 유입되고 동시에 열풍가열장치에 의하여 고온으로 가열된 가열공기를 혼입시켜 토출물을 발효시키는 발효단계와, A fermentation step of fermenting the discharged water by mixing heated air introduced by the storage bucket and heated at a high temperature by a hot air heater; 상기 발효단계를 통하여 발효된 발효물을 진공펌프로 인출하여 액비숙성조로 이송시켜 숙성시키는 숙성단계를 포함하는 것을 특징으로 하는 유기물의 발효처리방법The fermentation treatment method of the organic material, characterized in that it comprises a fermentation step of taking out the fermented product through the fermentation step with a vacuum pump to transfer to a liquid aging tank to ripen 유기물의 발효처리장치에 있어서,In the organic fermentation treatment apparatus, 상기 유기물의 발효처리장치(A)는, 분쇄기(11)가 내부에 회전가능하게 설치 되며 하부에는 침전물배출구(13)가 설치되고 하부에서 상방으로 경사지게 이송컨베어(12)가 설치된 저장조(1)와, The organic fermentation treatment device (A), the grinder 11 is rotatably installed therein and the reservoir (1) is provided with a sediment discharge port 13 in the lower portion and the conveying conveyor 12 is inclined upwardly from the bottom and , 상기 저장조(1)의 이송컨베어(12)가 상부에 설치되며 내부에는 페들형으로 복수의 페들이 종방향으로 설치된 분쇄기(21)가 회전가능하게 설치되며 하부에는 침전물이 배출되는 배출구(22)가 설치되며 상부의 중간에는 유기물의 토출물이 배출되는 토출구(23)가 형성되고, 상부에는 맨홀(24)이 형성되고 하부에는 공기를 불어 넣는 하부 블로어(25)가 설치되고, 하부에는 침전물이 배출되는 배출구(22)가 설치되고, 상기 블로어(25)의 상부에는 히터(26)가 설치되어 내부로 공급되는 공기를 70℃ 이상으로 가열하는 안정조(2)와, The conveying conveyor 12 of the reservoir 1 is installed on the upper part, and a grinder 21 in which a plurality of paddles are installed in the longitudinal direction in a pedestal shape is rotatably installed therein, and a discharge port 22 through which sediments are discharged. Discharge port 23 through which the discharge of organic matter is discharged is formed in the middle of the upper portion, a manhole 24 is formed in the upper portion, and a lower blower 25 for blowing air is provided in the upper portion, and the precipitate is discharged in the lower portion. The discharge port 22 is provided, the heater 26 is installed on the upper portion of the blower 25, the stabilizer (2) for heating the air supplied to the inside 70 ℃ or more, 토출구(23)의 하방에 배치되어 유기물이 수납되는 저장버켓(31)과, 상기 저장버켓(31)을 상방으로 이송시키도록 상기 저장버켓(31)이 배치되는 지지받침대(321)가 승강이동되는 운반기(32)가 구비된 토출물운반구(3)와, A storage bucket 31 disposed below the discharge port 23 to accommodate organic matter and a support support 321 on which the storage bucket 31 is disposed to move the storage bucket 31 upward are moved up and down. A discharge port carrying device 3 provided with a carrier 32, 상기 토출물운반구(3)의 저장호퍼(31)내의 토출물이 유입되는 유입구(41)가 원통형 몸체(40)의 상부에 설치되고 내부에는 교반기(42)가 회전가능하게 설치되고, 상기 교반기(42)는 리본형 타입이고, 구동축(421)을 통하여 5rpm ~ 30rpm의 저속으로 회전되고, 상기 원통형 몸체(40)의 상부에는 맨홀(43)이 설치되어 발효촉매제인 발효제와 발효대상물 중량의 0.2중량%인 균주를 혼합투입할 수 있고, 원통형 몸체(40)의 위로 상방에는 열교환기(44)가 설치되고, 원통형 몸체(40)의 상부의 측면에는 가스가 배출되는 가스배출구(45)가 설치되고 상기 가스배출구(45)를 통하여 배출가스가 배출되고 선단의 탈취부(46)가 구비된 발효조(4)와, An inlet 41 through which the discharge in the storage hopper 31 of the discharge port carrying port 3 flows is installed on the upper portion of the cylindrical body 40, and an agitator 42 is rotatably installed therein, and the agitator ( 42 is a ribbon type, rotated at a low speed of 5rpm ~ 30rpm through the drive shaft 421, the manhole 43 is installed on the upper portion of the cylindrical body 40 is 0.2 weight of the fermentation agent and fermentation weight of the fermentation catalyst % Of the strain can be mixed, the heat exchanger 44 is installed above the cylindrical body 40, the gas outlet 45 is installed on the side of the upper portion of the cylindrical body 40 is installed Fermentation tank 4 and the discharge gas is discharged through the gas discharge port 45 and the deodorizing portion 46 of the tip is provided, 상기 발효조(4)내에 고온공기를 공급하도록 하부에 급기블로워(51)가 설치되고 상부에 공기가열기(52)가 설치되고, 상기 공기가열기(52)의 배출부상에는 온도감지센서(53)가 설치된 고온공급기(5)와, An air supply blower 51 is installed at a lower portion of the fermentation tank 4 so as to supply high temperature air, and an air heater 52 is installed at an upper portion thereof, and a temperature sensor 53 is disposed on an outlet portion of the air heater 52. With a high temperature feeder (5) 상기 발효조(4)내의 발효물이 이송되어 상기 발효물을 숙성시키도록 바닥과 측면에 열선이 깔린 숙성조몸체(60)와, 상기 숙성조몸체(60)의 상부에는 상기 발효조(4)에서 연결되어 유기물이 공급되는 공급관(61)이 설치되고, 액비숙성조(6)의 내부에는 수중믹서기(62)가 설치되고, 측면에는 토출구(63)가 형성액비숙성조(6)를 포함하는 것을 특징으로 하는 유기물의 발효처리장치Fermentation product in the fermentation tank (4) is transferred to the mating bath body (60) with a heating wire on the bottom and side so as to ripen the fermentation product, the upper part of the mating bath body 60 is connected in the fermentation tank (4) And a supply pipe 61 through which the organic material is supplied, and an underwater mixer 62 is installed inside the liquid maturation tank 6, and a discharge port 63 is formed on the side thereof. Fermentation System for Organics
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108484241A (en) * 2018-05-30 2018-09-04 青岛金越隆机械有限公司 A kind of whole slot fermentation discharge system of organic fertilizer
CN110714636A (en) * 2019-11-14 2020-01-21 山东梦成环保科技有限公司 Integrated intelligent environmental protection toilet with vacuum manure suction and fermentation

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200417001Y1 (en) 2006-02-01 2006-05-24 김정태 Waste and Fecal Disposal Equipment Containing Organic Matter

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108484241A (en) * 2018-05-30 2018-09-04 青岛金越隆机械有限公司 A kind of whole slot fermentation discharge system of organic fertilizer
CN110714636A (en) * 2019-11-14 2020-01-21 山东梦成环保科技有限公司 Integrated intelligent environmental protection toilet with vacuum manure suction and fermentation

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