KR100752704B1 - Dehydrate method and natural dehydrate machine of wastes - Google Patents

Dehydrate method and natural dehydrate machine of wastes Download PDF

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KR100752704B1
KR100752704B1 KR1020050123894A KR20050123894A KR100752704B1 KR 100752704 B1 KR100752704 B1 KR 100752704B1 KR 1020050123894 A KR1020050123894 A KR 1020050123894A KR 20050123894 A KR20050123894 A KR 20050123894A KR 100752704 B1 KR100752704 B1 KR 100752704B1
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organic waste
storage hopper
oxygen
organic
waste storage
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KR1020050123894A
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KR20070063745A (en
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권태혁
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(주)그린니스
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/12Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
    • B30B9/14Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with only one screw or worm
    • 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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/125Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using screw filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/16Treatment of sludge; Devices therefor by de-watering, drying or thickening using drying or composting beds

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Molecular Biology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

본 발명은 음식물쓰레기 등의 유기성폐기물을 수거 운반하여 유기성폐기물의 자원화(전처리) 설비에 있어서의 반입된 유기성폐기물을 호퍼내에 톱밥과 함께 저장되도록 하고, 또한 상기 유기성폐기물의 호퍼내에 산소가 공급되도록 하면서, 배수파이프를 통하여 탈수토록하여, 호퍼내에 산소의 공급으로 폭기기능의 효율을 높여 탈리액의 오염을 최소화할 수 있으며, 또한 유기성폐기물의 유기질의 감소를 적절히 막아 중온 발효를 촉진시키어 유기성폐기물의 퇴비화 공정의 효율을 높일 수 있는 유기성폐기물의 자연탈수기에 관한 것으로, 유기성폐기물이나 고함수슬러지가 저장되는 유기성폐기물저장호퍼(10)와, 상기 유기성폐기물저장호퍼(10)에 배출스크류(30)가 설치되는 아래쪽에 자연 탈수된 여액이 집수되는 여액수집조에 있어서, 상기 유기성폐기물저장호퍼(10)내에 산소공급원과 연결되는 산소분출파이프(100)들이 등간격으로 세워 설치되고, 상기 산소분출파이프(100)들의 사이에 유기성폐기물의 탈수여액이 배출되도록 하는 배수파이프(200)들이 등간격으로 세워져 설치되어 있고, 또한 상기 유기성폐기물저장호퍼(10)내에 설치되는 산소분출파이프(100)에 산소분출구멍(110)들이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물에 산소가 공급되도록 되고, 유기성폐기물저장호퍼(10)내에 설치되는 배수파이프(200)에 배수구멍(210)이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물의 탈수여액이 여액수집조(20)로 배출되도록 되어 있으며, 또한 본 발명은 유기성폐기물저장호퍼(10)의 내벽에 톱밥(310)이 유지되도록 한 후, 유기성폐기물을 투입하고, 상기 유기성폐기물저장호퍼(10)의 유기성폐기물내에 산소가 주기적으로 공급되도록 하여, 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있도록 하고, 유기성폐기물의 탈수여액은 배수파이프(200)에 의하여 자연 낙하 탈수되어 유기성폐기물의 함수율을 최소화하여 하수처리장 허용부하 이하로 처리되도록 되어 있다. The present invention collects and transports organic wastes, such as food waste, so that the organic wastes introduced in the recycling (pretreatment) facility of organic wastes are stored together with sawdust in the hopper, and also oxygen is supplied into the hoppers of the organic wastes. , Dehydration through the drain pipe, supplying oxygen into the hopper to increase the efficiency of the aeration function to minimize the contamination of the desorption liquid, and also to prevent the reduction of organic waste of organic waste properly to promote moderate temperature fermentation to promote organic waste composting process It relates to a natural dehydrator of organic waste to increase the efficiency of the organic waste storage hopper 10 and the organic waste storage hopper 10, the organic waste storage hopper is stored, and the organic waste storage hopper 10 is installed In the filtrate collection tank in which the naturally dehydrated filtrate is collected at the bottom, the organic Oxygen ejection pipes 100 connected to the oxygen supply source are installed at equal intervals in the gas storage hopper 10, and a drain pipe 200 for discharging the dehydration liquid of the organic waste between the oxygen ejection pipes 100. Are installed at equal intervals, and the oxygen ejection holes 110 are drilled at equal intervals in the oxygen ejection pipe 100 installed in the organic waste storage hopper 10 to the organic waste in the organic waste storage hopper 10. Oxygen is supplied, and the drain hole 210 is drilled at equal intervals in the drain pipe 200 installed in the organic waste storage hopper 10 so that the dehydration liquid of the organic waste in the organic waste storage hopper 10 is filtered. 20), and the present invention after the sawdust 310 is maintained on the inner wall of the organic waste storage hopper 10, and put the organic waste, the organic waste storage Oxygen is periodically supplied into the organic waste of the hopper 10 to prevent the organic waste of organic waste from being appropriately reduced to promote fermentation, and the dehydration liquid of the organic waste is naturally dropped and dehydrated by the drain pipe 200. The water content of organic waste is minimized so that it can be treated under the allowable load of the sewage treatment plant.

유기성폐기물저장호퍼, 산소분출파이프, 산소분출구멍, 배수파이프, 배수구멍, 여액수집조 Organic waste storage hopper, oxygen jet pipe, oxygen jet hole, drain pipe, drain hole, filtrate collection tank

Description

유기성폐기물의 자연탈수기와 그의 탈수방법{Dehydrate method and natural dehydrate machine of wastes}Dehydration method and natural dehydrate machine of wastes

도 1 은 본 발명의 유기성폐기물의 자연탈수기의 종단면도,1 is a longitudinal sectional view of a natural dehydrator of an organic waste of the present invention,

도 2 는 본 발명의 유기성폐기물의 자연탈수기의 평면도,2 is a plan view of the natural dehydrator of the organic waste of the present invention,

도 3 는 본 발명의 유기성폐기물의 자연탈수기의 횡단면도,3 is a cross-sectional view of the natural dehydrator of the organic waste of the present invention,

도 4 는 도 2의 A-A선 단면도.4 is a cross-sectional view taken along the line A-A of FIG.

* 도면의 주요부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings

10 : 유기성폐기물저장호퍼 20 : 여액수집조10: organic waste storage hopper 20: filtrate collection tank

30 : 배출스크류 50 : 타공판30: discharge screw 50: punched plate

51 : 구멍 100 : 산소분출파이프51 hole 100 oxygen blowing pipe

110 : 산소분출구멍 120 : 연결파이프110: oxygen ejection hole 120: connection pipe

200 : 배수파이프 210 : 배수구멍200: drain pipe 210: drain hole

300 : 톱밥유지부재 310 : 톱밥300: sawdust holding member 310: sawdust

본 발명은 유기성폐기물 저장호퍼에서 유기성폐기물이 자연탈수되어 유기성폐기물의 함수율을 저감할 수 있는 유기성폐기물의 자연탈수기에 관한 것으로, 더욱 상세하게는 음식물쓰레기 등의 유기성폐기물을 수거 운반하여 유기성폐기물의 자원화(전처리) 설비에 있어서의 반입된 유기성폐기물을 호퍼내에 톱밥과 함께 저장되도록 하고, 또한 상기 유기성폐기물의 호퍼내에 산소가 공급되도록 하면서, 배수파이프를 통하여 탈수토록하여, 호퍼내에 산소의 공급으로 폭기기능의 효율을 높여 탈리액의 오염을 최소화할 수 있으며, 또한 유기성폐기물의 유기질의 감소를 적절히 막아 중온 발효를 촉진시키어 유기성폐기물의 퇴비화 공정의 효율을 높일 수 있는 유기성폐기물의 자연탈수기에 관한 것이다.The present invention relates to a natural dehydrator of organic wastes in which organic wastes are naturally dehydrated in an organic waste storage hopper to reduce the water content of organic wastes. More specifically, organic wastes are collected by transporting organic wastes such as food waste. (Pretreatment) The organic wastes carried in the equipment are stored together with sawdust in the hopper, and oxygen is supplied into the hopper of the organic wastes, and dehydrated through the drain pipe, thereby aeration function by supplying oxygen into the hopper. It is possible to minimize the contamination of the desorption liquid by increasing the efficiency of the organic waste, and also to prevent the organic waste of organic waste appropriately to promote the moderate temperature fermentation to increase the efficiency of the organic waste composting process of the organic waste natural dehydrator.

일반적으로 음식물쓰레기 등의 유기성폐기물은 퇴비나 사료로 재활용하기 위하여 유기성폐기물저장호퍼로부터 탈수 및 건조 등의 일련의 전처리과정이 필요하며 이때 탈수공정을 비롯한 대부분의 공정에서 탈수여액(침출수포함)이 발생하는데 이 탈수여액의 BOD, COD, SS의 함량이 크게 높아 별도의 폐수처리시설을 구비하여야 하나, 폐수처리시설자체가 오히려 음식물 전처리설비의 설비비용 보다 고가인 관계로, 초기시설투자비가 과다하게 투입된다는 문제가 있고, 또한 설비면적이 넓어서 넓은 설치 부지가 필요하게 된다.In general, organic wastes such as food waste require a series of pretreatment processes such as dehydration and drying from organic waste storage hoppers for recycling to compost or feed, and dehydration (including leachate) occurs in most processes including dehydration. However, the BOD, COD, and SS content of this dehydration solution is so high that a separate wastewater treatment facility should be provided. However, since the wastewater treatment facility itself is more expensive than the cost of food pretreatment facilities, the initial facility investment is excessive. There is a problem that the installation area is large, and a large installation site is required.

통상 수거운반된 유기성폐기물의 함수율은 88∼90%정도이며 함수율이 85%를 전, 후하는 고함수 슬러지 또는 유기성폐기물을 처리하기 위한 공정에서 이들을 이송시 벨트컨베이어, 스크류컨베이어의 동력을 이용한 배관 등을 많이 사용하나 벨트컨베이어는 함수율이 높아 이송효율이 떨어지고 주변을 오염시키는 문제점이 있고, 스크류컨베이어도 시간이 경과함에 따라 하부에 물이 차서 이송효율이 떨어지면서 유기성폐기물이나 고함수슬러지의 고형물이 되돌림되는 현상이 발생된다.In general, the water content of organic wastes collected and collected is about 88 ~ 90%, and the water content is 85% before and after the high-water sludge or the process for treating organic wastes. However, belt conveyor has a problem of contaminating the surrounding area due to high water content and consequently degrading the surrounding area. Also, screw conveyor also returns the organic waste or high content sludge solids as the water is filled at the lower part. Phenomenon occurs.

또한, 유기성폐기물 처리의 함수율 조절을 위한 방식으로서, 스크류프레스 및 원심탈수기 등을 이용한 강제 탈리하는 방식은 탈리액의 수질을 악화시켜, 하수처리장 연계처리시 부하량을 과도하게 증가시킬 수 있으며 하수처리장에서는 하수처리장 허용부하 이하로 폐수의 1차 처리를 요구하고 있는 실정이다. In addition, as a method for controlling the moisture content of the organic waste treatment, forced desorption using a screw press and a centrifugal dehydrator deteriorates the water quality of the desorption liquid, which can excessively increase the load during the sewage treatment plant-linked treatment. The situation is that the first treatment of wastewater is required below the allowable load of the treatment plant.

하지만, 유기성폐기물 탈리액의 1차 처리는 시설의 설치비용 및 운영비 면에서 경제적인 방식을 찾지 못한 실정이다. 더욱이 스크류프레스의 경우에 강제 이송에 따른 이송효율은 탁월하나 이송시 함수율이 저감되지 않으며 배관에 막힘 현상 발생시 전체 배관에 대한 보수 또는 공정의 중단이 불가피해질 수 있으며, 탈수설비의 용량이 필요이상 증량하여야 하는 문제가 제기된다.However, the primary treatment of organic waste stripping liquid has not found an economical method in terms of installation and operating costs. Moreover, in the case of screw press, the transfer efficiency due to the forced transfer is excellent, but the water content is not reduced during transfer, and if the blockage occurs in the pipe, repair or interruption of the entire pipe is inevitable, and the capacity of the dehydration facility is increased more than necessary. The question arises.

본 발명은 상기 문제를 해소하기 위한 것으로, 강제 탈수, 탈리방식이 아닌 자연탈수방식을 채택하며, 또한 호퍼내의 유기성폐기물에 산소의 주기적인 공급과 함께 배수파이프를 통하여 탈수여액이 자연스럽게 여액수집조로 배출될 수 있도록 함으로서, 호퍼내에 산소의 공급으로 폭기기능의 효율을 높여 탈리액의 오염을 최소화할 수 있으며, 또한 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있도록 함을 목적으로 한다. 또한 본 발명은 자연탈수에 의하여 유기성폐기물을 강제 탈수에 의한 수질악화를 방지하고, 또한 유기성폐기물의 함수율을 최소화하고 하수처리장 허용부하 이하로 폐수의 1차 처리로 인한 하수처리장의 부하량을 증가시킬 수 있도록 함을 목적으로 한다. The present invention is to solve the above problems, it adopts a natural dehydration method, not forced dehydration, desorption method, and dehydration filtrate is naturally discharged to the filtrate through the drain pipe with the periodic supply of oxygen to the organic waste in the hopper It is possible to minimize the contamination of the desorption liquid by increasing the efficiency of the aeration function by supplying oxygen into the hopper, and also to promote fermentation by appropriately preventing the reduction of organic matter of organic waste. In addition, the present invention can prevent the deterioration of water quality due to forced dehydration of organic waste by natural dehydration, and also to minimize the water content of organic waste and increase the load of the sewage treatment plant due to the first treatment of wastewater below the allowable load of the sewage treatment plant. The purpose is to make it work.

본 발명은 유기성폐기물이나 고함수슬러지가 저장되는 유기성폐기물저장호퍼와, 상기 유기성폐기물저장호퍼에 배출스크류가 설치되는 아래쪽에 자연 탈수된 여액이 집수되는 여액수집조에 있어서, 상기 유기성폐기물저장호퍼내에 산소공급원과 연결되는 산소분출파이프들이 등간격으로 세워 설치되고, 상기 산소분출파이프들의 사이에 유기성폐기물의 탈수여액이 배출되도록 하는 배수파이프들이 등간격으로 세워져 설치됨을 기본특징으로 한다.The present invention provides an organic waste storage hopper for storing organic wastes or high functional sludge, and a filtrate collection tank for collecting naturally dehydrated filtrates under which discharge screws are installed in the organic waste storage hopper, wherein oxygen is stored in the organic waste storage hopper. The basic feature is that the oxygen ejection pipes connected to the source are installed at equal intervals, and the drainage pipes are installed at equal intervals so that the dehydration liquid of organic waste is discharged between the oxygen ejection pipes.

또한, 본 발명의 상기 유기성폐기물저장호퍼내에 설치되는 산소분출파이프에 산소분출구멍들이 등간격으로 뚫려 유기성폐기물저장호퍼내의 유기성폐기물에 산소가 공급되도록 되고, 유기성폐기물저장호퍼내에 설치되는 배수파이프에 배수구멍이 등간격으로 뚫려 유기성폐기물저장호퍼내의 유기성폐기물의 탈수여액이 여액수집조로 배출되도록 되어 있다.In addition, oxygen ejection holes are drilled at equal intervals in the oxygen ejection pipe installed in the organic waste storage hopper of the present invention so that oxygen is supplied to the organic waste in the organic waste storage hopper, and drained to the drain pipe installed in the organic waste storage hopper. The holes are drilled at equal intervals so that the dehydration of organic waste in the organic waste storage hopper is discharged to the filtrate collection tank.

또한, 본 발명은 유기성폐기물저장호퍼의 내벽에 톱밥이 유지되도록 한 후, 유기성폐기물을 투입하고, 상기 유기성폐기물저장호퍼의 유기성폐기물내에 산소가 주기적으로 공급되도록 하여, 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있도록 하고, 유기성폐기물의 탈수여액은 배수파이프에 의하여 자연 낙하 탈수되어 유기성폐기물의 함수율을 최소화하여 하수처리장 허용부하 이하로 처리되도록 한 유기성폐기물의 자연탈수방법을 특징으로 한다. In addition, the present invention is to maintain the sawdust on the inner wall of the organic waste storage hopper, the organic waste is introduced, and the oxygen is periodically supplied into the organic waste of the organic waste storage hopper, to appropriately reduce the organic waste of organic waste It is possible to promote fermentation, and the dehydration liquid of organic wastes is characterized by the natural dehydration method of organic wastes which are naturally dropped and dehydrated by drainage pipe to minimize the water content of organic wastes and to be treated below the allowable load of the sewage treatment plant.

본 발명의 실시예를 첨부도면에 의하여 상세히 설명하면 다음과 같다.An embodiment of the present invention will be described in detail with reference to the accompanying drawings.

도 1 은 본 발명의 유기성폐기물의 자연탈수기의 종단면도이고, 또한 도 2 는 본 발명의 유기성폐기물의 자연탈수기의 평면도이며, 또한 도 3 는 본 발명의 유기성폐기물의 자연탈수기의 횡단면도이고, 또한 도 4 는 도 2의 A-A선 단면도이다.1 is a longitudinal cross-sectional view of a natural dehydrator of an organic waste of the present invention, and FIG. 2 is a plan view of a natural dehydrator of an organic waste of the present invention, and FIG. 3 is a cross-sectional view of a natural dehydrator of an organic waste of the present invention. 4 is a cross-sectional view taken along the line AA of FIG. 2.

본 발명의 유기성폐기물저장호퍼(10)는 트럭 등의 운송수단에 의하여 운송되어온 유기성폐기물을 호퍼에 투입하여 산소의 공급과 유기성폐기물의 침출수를 여액수집조(20)로 배출토록 한다.The organic waste storage hopper 10 of the present invention injects organic waste transported by a vehicle such as a truck into a hopper to discharge oxygen and leachate of organic waste into the filtrate collection tank 20.

특히, 본 발명은 유기성폐기물이나 고함수슬러지가 저장되는 유기성폐기물저장호퍼(10)에는 아래쪽에 구동원(도시생략)과 연결되어 구동되는 배출스크류(30)들이 설치되어 있으며, 이 배출스크류(30)들의 아래쪽에는 유기성폐기물저장호퍼(10)내의 유기성폐기물의 탈수여액이 자연적으로 탈수된 여액이 집수되는 여액수집조(20)가 형성되어 있다.In particular, the present invention, the organic waste storage hopper 10, which stores organic waste or high functional sludge, is provided with a discharge screw 30 is connected to the drive source (not shown) in the bottom, the discharge screw 30 At the bottom of the filter, a filtrate collection tank 20 is formed in which the dehydrated filtrate of the organic waste in the organic waste storage hopper 10 is naturally dehydrated.

상기 배출스크류(30)의 아래에는 도 1 및 도 4에 나타낸 바와 같이 구멍(51)이 등간격으로 뚫려 형성된 타공판(50)이 형성되어, 이 타공판(50)을 통하여 여액이 여액수집조(20)로 집수된다.1 and 4, the perforated plate 50 formed by opening the holes 51 at equal intervals is formed below the discharge screw 30, and the filtrate collects the filtrate through the perforated plate 50. Is collected.

그리고, 상기 여액수집조(20)에는 이송배관(21)이 연결되며, 이 이송배관(21)은 상기 여액저장조(도시생략)와 연결되어, 여액을 여액저장조(도시생략)로 이동시키게 된다.In addition, the filtrate collection tank 20 is connected to the transfer pipe 21, the transfer pipe 21 is connected to the filtrate storage tank (not shown), to move the filtrate to the filtrate storage tank (not shown).

또한, 상기 배출스크류(30)에는 이송스크류컨베이어(40)가 연결되어 자연탈수된 유기성폐기물을 다음의 공정으로 이송시키게 된다.In addition, the transfer screw conveyor 40 is connected to the discharge screw 30 to transfer the organic dehydrated organic waste to the next process.

본 발명은 도 1 내지 도 4에 나타낸 바와 같이 유기성폐기물이나 고함수슬러지가 저장되는 유기성폐기물저장호퍼(10)와, 상기 유기성폐기물저장호퍼(10)에 배출스크류(30)가 설치되는 아래쪽에 자연 탈수된 여액이 집수되는 여액수집조(20)로 이루어진 탈수기에 있어서의 상기 유기성폐기물저장호퍼(10)내에 산소공급원과 연결되는 산소분출파이프(100)들이 등간격으로 세워 설치되고, 상기 산소분출파이프(100)들의 사이에 유기성폐기물의 탈수여액이 배출되도록 하는 배수파이프(200)들이 등간격으로 세워져 설치되어 있다.1 to 4, the organic waste storage hopper 10 in which organic waste or high functional sludge is stored, and the discharge screw 30 in the organic waste storage hopper 10 are installed in the lower portion. In the organic waste storage hopper 10 in the dehydrator consisting of the filtrate collection tank 20 in which the dehydrated filtrate is collected, oxygen ejection pipes 100 connected to an oxygen supply source are installed at equal intervals, and the oxygen ejection pipe The drain pipes 200 are installed at equal intervals so that the dehydration liquid of the organic waste is discharged between the (100).

즉, 본 발명의 상기 유기성폐기물저장호퍼(10)내에 설치되는 산소분출파이프(100)에 산소분출구멍(110)들이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물에 산소가 공급되도록 한다.That is, the oxygen ejection holes 110 are drilled at equal intervals in the oxygen ejection pipe 100 installed in the organic waste storage hopper 10 of the present invention so that oxygen is supplied to the organic waste in the organic waste storage hopper 10. .

상기 유기성폐기물저장호퍼(10)내에 산소의 공급은 호퍼내에 산소의 공급으로 폭기기능의 효율을 높여 탈리액의 오염을 최소화할 수 있다.The supply of oxygen into the organic waste storage hopper 10 can minimize the contamination of the desorption liquid by increasing the efficiency of the aeration function by the supply of oxygen into the hopper.

또한, 유기성폐기물저장호퍼(10)내에 설치되는 배수파이프(200)에 배수구멍(210)이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물의 탈수여액이 여액수집조(20)로 배출되게 된다. In addition, drain holes 210 are drilled at equal intervals in the drain pipe 200 installed in the organic waste storage hopper 10 so that the dehydration liquid of organic waste in the organic waste storage hopper 10 is discharged to the filtrate collection tank 20. Will be.

상기 산소분출파이프(100)들은 길이방향의 등간격으로 산소분출구멍(110)들이 다수 뚫려 산소공급원(도시생략)으로부터 산소가 공급되어 산소분출구멍(110)을 통하여 유기성폐기물에 산소가 공급될 수 있도록 되어 있으며, 산소공급원으로부터 의 산소는 산소분출파이프(100) 아래쪽에 연결된 연결파이프(120)를 통하여 아래쪽에서 위쪽으로 분출된다. 상기 산소분출파이프(100)의 위쪽은 폐쇄되어 산소가 산소분출구멍(110)을 통해 분출될 수 있도록 한다.The oxygen ejection pipes 100 may be supplied with oxygen from an oxygen supply source (not shown) through a plurality of oxygen ejection holes 110 at equal intervals in the longitudinal direction, and oxygen may be supplied to the organic waste through the oxygen ejection hole 110. The oxygen from the oxygen supply source is ejected from the bottom through the connecting pipe 120 connected to the bottom of the oxygen ejection pipe 100. The upper portion of the oxygen ejection pipe 100 is closed to allow oxygen to be ejected through the oxygen ejection hole 110.

상기 산소분출구멍(110)은 유기성폐기물에 의하여 막히는 것을 방지하도록 하기 위하여 구멍의 주위에 보호커버(도시생략) 등을 형성할 수 있다. The oxygen ejection hole 110 may form a protective cover (not shown) or the like around the hole in order to prevent it from being blocked by organic waste.

또한, 산소에 열을 가하여 유기성폐기물저장호퍼(10)내의 유기성폐기물의 유기질의 감소를 막아 발효를 촉진시킬 수 있다.In addition, by applying heat to the oxygen to prevent the organic waste of the organic waste in the organic waste storage hopper 10 can be promoted to fermentation.

또한, 배수파이프(200)는 둘레면에 배수구멍(210)이 등간격으로 뚫려서 유기성폐기물저장호퍼(10)내의 유기성폐기물의 탈수여액이 배출되도록 한다. 상기 탈수여액은 상기 배수구멍(210)을 통해 유기성폐기물저장호퍼(10)의 아래쪽으로 자연탈수 되도록 하며, 상기 배출스크류(30)의 아래의 타공판(50)의 구멍(51)을 통하여 여액수집조(20)로 집수케 한다. In addition, the drain pipe 200 is a drain hole 210 is drilled at equal intervals on the circumferential surface so that the dehydration liquid of the organic waste in the organic waste storage hopper 10 is discharged. The dehydration filtrate is naturally dehydrated to the bottom of the organic waste storage hopper 10 through the drain hole 210, the filtrate collection tank through the hole 51 of the perforated plate 50 below the discharge screw 30 (20).

상기 배수파이프(200)의 배수구멍(210) 역시 유기성폐기물에 의하여 막히는 것을 방지하도록 하기 위하여 구멍의 주위에 보호커버(도시생략) 등을 형성할 수 있다.In order to prevent the drainage hole 210 of the drainage pipe 200 from being blocked by organic waste, a protective cover (not shown) may be formed around the hole.

또한, 상기 산소분출파이프(100)들과 배수파이프(200)들은 유기성폐기물저장호퍼(10)내에서 안정적으로 세워 설치될 수 있도록 고정브라켓(60)에 의하여 유지 고정되어 있다.In addition, the oxygen ejection pipes 100 and the drainage pipes 200 are held and fixed by the fixing bracket 60 so that they can be installed stably in the organic waste storage hopper 10.

또한, 유기성폐기물저장호퍼(10)의 내벽에는 톱밥(310)을 유지할 수 있는 톱밥유지부재(300)들이 형성되어 유기성폐기물저장호퍼(10)내에 유기성폐기물을 투입하기 전에 유기성폐기물저장호퍼(10)의 내벽에 톱밥이 형성되도록 하여 유기성폐기물에 포함되어 있는 탈수여액의 배출이 용이하도록 한다.In addition, sawdust holding members 300 are formed on the inner wall of the organic waste storage hopper 10 so that the organic waste storage hopper 10 may be disposed before the organic waste is stored in the organic waste storage hopper 10. Sawdust is formed on the inner wall of the to facilitate the discharge of the dehydration liquid contained in the organic waste.

상기 톱밥유지부재(300)에 대하여 특별히 한정하는 것은 아니며 유기성폐기물저장호퍼(10)내에 톱밥이 유지될 수 있는 형태이면 된다. 또한 톱밥은 유기성폐기물에 포함되어 있는 탈수여액의 배출이 용이하도록 하기 때문에 유기성폐기물저장호퍼(10)의 바닥부분에는 반드시 설치하는 것이 유리하다. The sawdust holding member 300 is not particularly limited and may be any shape in which sawdust may be maintained in the organic waste storage hopper 10. In addition, the sawdust is advantageous to be necessarily installed in the bottom portion of the organic waste storage hopper 10 because it facilitates the discharge of the dehydration liquid contained in the organic waste.

또한, 상기 자연탈수 후 나온 탈리액은 정수장치에 보내어 정수하여 방출한다.In addition, the desorption liquid after the natural dehydration is sent to a water purifier to purify and discharged.

실험예Experimental Example

본 발명은 유기성폐기물저장호퍼(10)의 내벽에 톱밥(310)이 유지되도록 한 후, 유기성폐기물을 투입하고, 상기 유기성폐기물저장호퍼(10)의 유기성폐기물내에 산소가 주기적으로 공급되도록 하여, 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있고, 유기성폐기물의 탈수여액은 배수파이프(200)에 의하여 자연 낙하 탈수되어 유기성폐기물의 함수율을 최소화하여 하수처리장 허용부하 이하로 처리되도록 할 수 있었다.According to the present invention, after the sawdust 310 is maintained on the inner wall of the organic waste storage hopper 10, the organic waste is introduced, and oxygen is periodically supplied into the organic waste of the organic waste storage hopper 10. Fermentation can be promoted by appropriately preventing the reduction of organic matter of the waste, and the dehydration liquid of organic waste can be naturally dropped and dehydrated by the drain pipe 200 to minimize the moisture content of the organic waste so that it can be treated below the allowable load of the sewage treatment plant. .

본 발명은 강제탈리 방식이 아닌 자연탈수 및 정화장치 시험을 실시하게 되었으며, LAB TEST결과 비교적 만족한 결과를 얻게 되었다.In the present invention, a natural dehydration and purification apparatus test was performed, not forced desorption, and a relatively satisfactory result was obtained.

또한, 자연탈리방식은 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있을 것으로 예상된다. In addition, the natural desorption method is expected to be able to promote the fermentation by properly preventing the organic waste of organic waste.

테스트 방법Test method

반입된 유기성폐기물(함수율 : 82%)를 톱밥(함수율 : 약30%)과 혼합한 후 공기공급장치가 설치된 유기성폐기물저장호퍼에 5일간 중온발효 시키면서 얻은 시료를 활용하여 유기성폐기물의 함수율 및 폐수성상을 측정하였다. After mixing the imported organic waste (water content: 82%) with sawdust (water content: about 30%), the moisture content and wastewater phase of organic wastes were collected by using the sample obtained by fermenting the organic waste storage hopper with air supply for 5 days at medium temperature. Was measured.

<LAB TEST> <LAB TEST>

장비투입량 : 유기성폐기물(83㎏)+톱밥(6.5㎏) = 89.5㎏ (부자재 투입율 : 7.3%)Equipment input amount: organic waste (83㎏) + sawdust (6.5㎏) = 89.5㎏ (subsidiary material input rate: 7.3%)

공기공급 주기 : 5분 경과후 1분간 공급 Air supply cycle: 1 minute after 5 minutes

시험결과Test result

탈리액 발생 (자체측정) Desorption solution generation (self-measurement)

일 시Pause 발생량 (㎏)Generation amount (㎏) 일 시Pause 발생량 (㎏)Generation amount (㎏) 11/12 (14:00)11/12 (14:00) 3.23.2 11/13 (09:00)11/13 (09:00) 5.95.9 11/12 (16:00)11/12 (16:00) 1.41.4 11/14 (09:30)11/14 (09:30) 2.42.4 계 (침출수량)Total (leaching quantity) 12.912.9 증발량 (㎏)Evaporation amount (㎏) 11.211.2

탈리액의 수질변화 (시험방법 ; 수질공정시험법, (주)케이비엔텍)Changes in Water Quality of Tally Solution (Test Method; Water Process Test, KB Entec Co., Ltd.)

구 분division 시험항목Test Items pHpH CODcrCODcr BODBOD SSSS N-H (광물)N-H (mineral) N-H (동물)N-H (Animals) T-NT-N T-PT-P ClCl 함수율Water content 스크류프레스 (A)Screw Press (A) 시험값 (㎏/ℓ)Test value (㎏ / ℓ) 4.354.35 146,000146,000 88,12588,125 61,00061,000 1616 12,00012,000 3,8643,864 614.9614.9 5,565.75,565.7 73.9(%)73.9 (%) 원심탈수기 (B)Centrifugal Dehydrator (B) 시험값 (㎏/ℓ)Test value (㎏ / ℓ) 4.274.27 144,000144,000 76,87576,875 27,10027,100 1212 10,50010,500 3,155.23,155.2 573.1573.1 5,069.45,069.4 66.2(%)66.2 (%) 제거율Removal rate -- 1.37%1.37% 12.8%12.8% 55.6%55.6% 25.0%25.0% 12.5%12.5% 18.3%18.3% 6.8%6.8% 8.9%8.9% 10.4%10.4% 시험장비 [(A-C)/A]* 100(%)Test Equipment [(A-C) / A] * 100 (%) 시험값 (㎏/ℓ)Test value (㎏ / ℓ) 4.484.48 38,75038,750 24,00024,000 990   990 0.80.8 30    30 610.8610.8 148.1148.1 2,233.42,233.4 67.7(%)67.7 (%) 개선율Improvement -- 73.5%73.5% 72.8%72.8% 98.4%98.4% 95.0%95.0% 99.8%99.8% 84.2%84.2% 75.975.9 59.9%59.9% 8.4%8.4%

취출물   Extract

파쇄선별후After crushing 스크류프레스탈리액Screw presse liquid 원심탈수 탈리액Centrifugal dewatering solution 시설 5일 경과후After 5 days of facility 여과후 산발효 상태Acid fermentation after filtration

Figure 112005073429059-pat00001
Figure 112005073429059-pat00001
Figure 112005073429059-pat00002
Figure 112005073429059-pat00002
Figure 112005073429059-pat00003
Figure 112005073429059-pat00003
Figure 112005073429059-pat00004
Figure 112005073429059-pat00004
Figure 112005073429059-pat00005
Figure 112005073429059-pat00005
액상+고형물Liquid + Solid 테스트 의뢰Request a test

고형물의 함수율 변화 (시험방법 ; 수질공정시험법, (주)케이비엔텍)Water content change of solids (Test Method; Water Process Test, KB Entec Co., Ltd.)

- 테스트 전 음식물의 함수율 : 82% -Water content of food before test: 82%

- 테스트(약 5일 경과) 후 함수율 : 67.7% (※TEST REPORT 참조) -Water content after test (about 5 days): 67.7% (Refer to ※ TEST REPORT)

결론conclusion

본 시험 결과 폐수수질은 각 항목별로 70%이상의 오염도 제거 효과를 보였으며, 함수율은 68%선으로 조절되어 만족할 만한 결과를 얻게 되었으며 향후 본 설비의 상용화 (Pilot설비 등) 및 유기성폐기물 퇴비화 공정의 재구성 등을 추진해 나갈 것이다.As a result of this test, wastewater quality showed more than 70% pollution removal effect for each item, and the water content was adjusted to 68% line to obtain satisfactory results. Future commercialization of this facility (Pilot facility, etc.) and reorganization of organic waste composting process I will push forward.

이상과 같이, 본 발명은 음식물쓰레기 등의 유기성폐기물을 수거 운반하여 유기성폐기물의 자원화(전처리) 설비에 있어서의 반입된 유기성폐기물을 호퍼내에 톱밥과 함께 저장되도록 하고, 또한 상기 유기성폐기물의 호퍼내에 산소가 공급되도록 하면서, 배수파이프를 통하여 탈수토록하여, 호퍼내에 산소의 공급으로 폭기기능의 효율을 높여 탈리액의 오염을 최소화할 수 있으며, 또한 유기성폐기물의 유기질의 감소를 적절히 막아 중온 발효를 촉진시키어 유기성폐기물의 퇴비화 공정의 효율을 높일 수 있다.As described above, the present invention collects and transports organic wastes such as food waste, so that the organic wastes carried in the resource (pretreatment) facility of organic wastes are stored together with sawdust in a hopper, and also oxygen in the hopper of the organic wastes. By supplying oxygen, it is possible to dehydrate through the drain pipe, supplying oxygen into the hopper to increase the efficiency of the aeration function, thereby minimizing the contamination of the desorption liquid, and promoting moderate temperature fermentation by appropriately preventing the reduction of organic waste of organic waste. The efficiency of the waste composting process can be improved.

Claims (3)

유기성폐기물이나 고함수슬러지가 저장되는 유기성폐기물저장호퍼(10)와, 상기 유기성폐기물저장호퍼(10)에 배출스크류(30)가 설치되는 아래쪽에 자연 탈수된 여액이 집수되는 여액수집조에 있어서, In a filtrate collection tank in which an organic waste storage hopper (10) storing organic waste or a high water content sludge and a naturally dehydrated filtrate are collected in a lower portion where the discharge screw (30) is installed in the organic waste storage hopper (10). 상기 유기성폐기물저장호퍼(10)내에 산소공급원과 연결되는 산소분출파이프(100)들이 등간격으로 세워 설치되고, 상기 산소분출파이프(100)들의 사이에 유기성폐기물의 탈수여액이 배출되도록 하는 배수파이프(200)들이 등간격으로 세워져 설치됨을 특징으로 하는 유기성폐기물의 자연탈수기.Oxygen ejection pipes 100 connected to the oxygen supply source are installed at equal intervals in the organic waste storage hopper 10, and drain pipes for discharging the dehydration liquid of organic wastes between the oxygen ejection pipes 100 ( Natural dehydrator of organic waste, characterized in that the 200 is installed at equal intervals. 제 1 항에 있어서, 상기 유기성폐기물저장호퍼(10)내에 설치되는 산소분출파이프(100)에 산소분출구멍(110)들이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물에 산소가 공급되도록 되고, 유기성폐기물저장호퍼(10)내에 설치되는 배수파이프(200)에 배수구멍(210)이 등간격으로 뚫려 유기성폐기물저장호퍼(10)내의 유기성폐기물의 탈수여액이 여액수집조(20)로 배출되도록 됨을 특징으로 하는 유기성폐기물의 자연탈수기.According to claim 1, Oxygen ejection holes 110 are drilled at equal intervals in the oxygen jet pipe 100 installed in the organic waste storage hopper 10 so that oxygen is supplied to the organic waste in the organic waste storage hopper 10. The drain holes 210 are drilled at equal intervals in the drain pipe 200 installed in the organic waste storage hopper 10, and the dehydration liquid of the organic waste in the organic waste storage hopper 10 is discharged to the filtrate collection tank 20. Natural dehydrator, characterized in that the organic waste. 유기성폐기물저장호퍼(10)의 내벽에 톱밥(310)이 유지되도록 한 후, 유기성폐기물을 투입하고, 상기 유기성폐기물저장호퍼(10)의 유기성폐기물내에 산소가 주기적으로 공급되도록 하여, 유기성폐기물의 유기질의 감소를 적절히 막아 발효를 촉진시킬 수 있도록 하고, 유기성폐기물의 탈수여액은 배수파이프(200)에 의하여 자연 낙하 탈수되어 유기성폐기물의 함수율을 최소화하여 하수처리장 허용부하 이하로 처리되도록 됨을 특징으로 하는 유기성폐기물의 자연탈수방법.After the sawdust 310 is maintained on the inner wall of the organic waste storage hopper 10, the organic waste is introduced, and oxygen is periodically supplied into the organic waste of the organic waste storage hopper 10, so that organic matter of organic waste It is possible to prevent fermentation by appropriately to promote fermentation, and the organic waste dehydration liquid is naturally dropped and dehydrated by the drain pipe 200 to minimize the moisture content of the organic waste to be treated below the allowable load of the sewage treatment plant. Natural Dewatering Method of Waste.
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KR102198208B1 (en) 2020-07-13 2021-01-04 채재우 A lot of water waste recycling and incineration equipment

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19980044964A (en) * 1996-12-09 1998-09-15 지경준 Organic waste disposal method and device
KR0153510B1 (en) * 1995-08-02 1998-11-16 주용수 A compost fermentation device for waste food
KR20010027512A (en) * 1999-09-14 2001-04-06 노현수 crusher of refuse
KR20030006688A (en) * 2001-07-14 2003-01-23 주식회사 그렌지 Treatment system for organic waste matter and the method thereof
KR200355907Y1 (en) * 2004-04-20 2004-07-09 한태원 Multirole fermenter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR0153510B1 (en) * 1995-08-02 1998-11-16 주용수 A compost fermentation device for waste food
KR19980044964A (en) * 1996-12-09 1998-09-15 지경준 Organic waste disposal method and device
KR20010027512A (en) * 1999-09-14 2001-04-06 노현수 crusher of refuse
KR20030006688A (en) * 2001-07-14 2003-01-23 주식회사 그렌지 Treatment system for organic waste matter and the method thereof
KR200355907Y1 (en) * 2004-04-20 2004-07-09 한태원 Multirole fermenter

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102198208B1 (en) 2020-07-13 2021-01-04 채재우 A lot of water waste recycling and incineration equipment

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