KR20080025386A - Anaerobic digestion apparatus for semi-liquid organic waste treatment - Google Patents

Anaerobic digestion apparatus for semi-liquid organic waste treatment Download PDF

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KR20080025386A
KR20080025386A KR20080015913A KR20080015913A KR20080025386A KR 20080025386 A KR20080025386 A KR 20080025386A KR 20080015913 A KR20080015913 A KR 20080015913A KR 20080015913 A KR20080015913 A KR 20080015913A KR 20080025386 A KR20080025386 A KR 20080025386A
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digester
shaft
semi
pipe
anaerobic digestion
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KR100836149B1 (en
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윤중현
박완섭
정찬기
전영봉
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주식회사 도화종합기술공사
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    • 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
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

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Abstract

An anaerobic digestion apparatus for generating digestion gas by degrading semi-liquid organic waste such as food waste and livestock waste is provided to improve treatment efficiency of the anaerobic digestion apparatus, reduce required volume and retention time compared with the treatment capacity, enable digestion gas to be used as fuel, and produce a compost from a treated material of the anaerobic digestion apparatus. An anaerobic digestion apparatus for semi-liquid organic waste treatment comprises: a plurality of perforated plates(141) which are installed in a stand pipe(140) such that the perforated plates cross an inner part of the stand pipe, and in which a plurality of through-holes(142) are formed; an agitation shaft(210) installed in a central part of a digestion tank(100) and driven by a drive motor(290); a traveling ring(205) which is installed along an inner peripheral surface of a lower part of the digestion tank such that the traveling ring is concentric to the agitation shaft; a lateral shaft(201) installed on a lower end of the agitation shaft perpendicularly to the agitation shaft; and hollow shafts(202) which are rotatably joined the lateral shaft, and which have a traveling wheel(204) formed on front ends thereof, and a plurality of agitation vanes(203) formed on outer peripheral surfaces thereof so as to rotate simultaneously the agitation vanes about the agitation shaft as well as the lateral shaft by rotating the agitation shaft, thereby rotating the traveling wheels along the traveling ring.

Description

반액상 유기 폐기물 처리용 혐기성 소화장치{Anaerobic digestion apparatus for semi-liquid organic waste treatment}Anaerobic digestion apparatus for semi-liquid organic waste treatment

본 발명은 음식물 또는 축산 폐기물 등의 반액상 유기폐기물을 분해하여 소화가스를 발생시키는 혐기성 소화장치에 관한 것으로, 소화장치 내부의 입상관에 다공판을 설치하여 폐기물의 소화장치내 유동과정에서의 혼합효율을 향상시키고, 교반기의 교반익을 수직 및 수평면상 복합 회전이 가능하도록 구성함으로써 교반효율을 배가한 것이다.The present invention relates to an anaerobic digestion apparatus that generates digestive gas by decomposing semi-liquid organic waste such as food or livestock waste, and installs a porous plate in a granulation pipe inside the extinguishing system to mix waste in the flow process of the extinguishing system. The efficiency was improved, and the stirring blades of the stirrer were doubled by being configured to allow the combined rotation of the vertical and horizontal planes.

혐기성 소화법(Anaerobic digestion)은 음식물, 축산 폐기물, 하수슬러지, 분뇨 및 고농도 유기성 공장폐수 등의 안정화를 위한 생물학적 처리법으로서, 혐기성 조건하에서 통성혐기성균 및 절대혐기성균의 작용으로 고분자 유기물을 가수분해하여 초산(Acetic acid), 프로피온산(Propionic acid), 낙산(Butric acid) 등의 휘발성 지방산을 생성하고, 최종적으로 메탄, 이산화탄소, 암모니아 및 황화수소로 가스화하는 처리법을 말한다.Anaerobic digestion is a biological treatment method for stabilization of food, livestock waste, sewage sludge, manure and high concentration of organic plant wastewater. It refers to a treatment that produces volatile fatty acids such as acetic acid, propionic acid, butyric acid, and finally gasifies methane, carbon dioxide, ammonia and hydrogen sulfide.

이러한 혐기성 소화법은 단위 유기물당 발생되는 생물학적 슬러지량이 호기성처리기법에 비하여 현저히 적고, 배출되는 소화가스내에 연료화가 가능한 메탄이 상당비율 포함되며, 소화슬러지에는 질소, 인 및 부식질이 풍부하여 비료가치가 높은 장점이 있어, 단순한 폐기물의 분해, 처리기능외에도 연료 및 퇴비를 생산하는 친환경 자원재생산 처리기법으로서 각광받고 있다.In this anaerobic digestion method, the amount of biological sludge generated per unit organic matter is significantly lower than that of aerobic treatment, and the methane that can be fuelized in the exhaust gas is contained. The digested sludge is rich in nitrogen, phosphorus, and humus, so that fertilizer value is high. Due to its high advantages, it has been spotlighted as an eco-friendly resource recycling processing technique that produces fuel and compost in addition to simple decomposition and treatment of waste.

도 1은 혐기성 소화법을 통하여 반액상(半液狀), 반고상(半固狀) 유기성 폐기물을 처리하는 과정을 간략히 도시한 것으로, 처리시설로 반입된 폐기물은 파쇄설비 및 선별설비를 거치면서 불순물이 제거된 페이스트(paste) 상태로 처리되고, 이후 혐기성 소화장치에서 소화가스, 상등수(上等水) 및 소화슬러지로 분해처리된다.Figure 1 is a simplified illustration of the process of processing semi-liquid, semi-solid organic waste through the anaerobic digestion method, while the waste brought into the treatment facility goes through the crushing and sorting equipment It is treated in the form of a paste from which impurities are removed and then decomposed into digestive gas, supernatant water and digested sludge in an anaerobic digester.

도 2는 종래 혐기성 소화장치의 대표단면도로서, 내부에 입상관(140)이 설치된 밀폐 원형 수조식 소화장치가 예시되어 있는데, 유입관(111)을 통하여 입상관(140) 내부로 유입된 반액상 폐기물은 입상관(140)을 통하여 소화조(100) 하부로 이동하며, 이후 소화조(100) 하부 소화슬러지내 미생물에 의하여 상등수와 가스로 분해된다.Figure 2 is a representative cross-sectional view of the conventional anaerobic digestion apparatus, there is illustrated a sealed circular tank type fire extinguishing device installed granular tube 140 therein, the semi-liquid waste introduced into the granular tube 140 through the inlet tube 111 Is moved to the digestion tank 100 through the granular pipe 140, and is then decomposed into the supernatant and gas by the microorganisms in the digestion sludge lower digestive tank 100.

소화조(100) 하부에는 구동모터(290)로 구동되는 교반기(200)가 설치되어 폐기물의 교반 및 상층 소화슬러지와의 혼합을 촉진하게 되며, 소화조(100)의 덮개(120)에는 배기관(121)이 설치되어 소화가스를 외부로 배출하게 된다.A stirrer 200 driven by the driving motor 290 is installed at the lower part of the digester 100 to promote agitation of the waste and mixing with the upper extinguishing sludge, and the exhaust pipe 121 is disposed on the cover 120 of the digester 100. This is installed to discharge the extinguishing gas to the outside.

또한, 소화조(100)의 상부에는 소화조(100)를 포위하는 환형수로(130)가 설치되어 소화조(100) 상단을 월류(越流)한 상등수가 집수되어 배수관(112)을 통하여 배출되고, 소화조(100)의 하단부에는 배출관(113)이 형성되어 잉여 소화슬러지를 배출하게 된다.In addition, the upper part of the digester 100 is provided with an annular water channel 130 surrounding the digester 100 is collected, the supernatant water overflowing the upper end of the digester 100 is collected and discharged through the drain pipe 112, A discharge pipe 113 is formed at the lower end of the digester 100 to discharge excess digested sludge.

전술한 바와 같은 종래의 혐기성 소화장치는 소화조(100) 내부에 설치된 입상관(140)을 통하여 유입된 반액상 폐기물이 하강하면서 소화조(100) 하부 소화슬러지와의 접촉을 유도하는 방식으로서, 함수비가 낮은 반액체, 반고체 상태인 처리대상 폐기물의 특성상 매우 느린 속도로 입상관(140) 내 하강이 이루어지므로, 이러한 소화조(100) 내 폐기물의 유동과정에서 비중차에 의한 구성성분의 불요(不要) 분리가 발생될 수 있을 뿐 아니라, 미생물에 의한 분해작용이 왕성한 소화조(100) 하부 폐기물 및 소화슬러지와의 혼합 또한 원활하지 못한 문제점이 있었다.The conventional anaerobic digestion apparatus as described above is a method of inducing contact with the digestion sludge under the digester 100 while the half-liquid waste introduced through the granular pipe 140 installed inside the digester 100 is lowered. Due to the low semi-liquid and semi-solid state of the waste to be treated, the descent in the granular pipe 140 occurs at a very slow rate, and thus, separation of components due to specific gravity differences in the flow of the waste in the digester 100 occurs. Not only may be generated, but the mixing and digestion of the digestion sludge under the digestion tank 100 having a strong decomposition by the microorganisms also had a problem that is not smooth.

즉, 종래의 혐기성 소화장치내 입상관(140)은 소화조(100) 중심부에 수직으로 설치된 관체로서, 입상관(140)으로 유입된 반액상 폐기물은 입상관(140)을 통하여 소화조(100) 하부로 서서히 하강하게 되는데 입상관(140)의 구조상 하강과정이 매우 안정된 상태로 진행되므로 폐기물의 교란이 거의 발생하지 않으며, 따라서 폐기물을 구성하는 물, 고형분 및 지질 등이 분리될 수 있는 것이다.That is, the conventional anaerobic digestion apparatus in the granular tube 140 is a tube installed vertically in the center of the digester 100, the semi-liquid waste introduced into the granular tube 140 is lower than the digester 100 through the granular tube 140 As it gradually descends, the structure of the granular pipe 140 proceeds in a very stable state, so that the disturbance of the waste hardly occurs, and thus water, solids and lipids constituting the waste can be separated.

또한, 하강된 폐기물이 소화조(100) 하부의 소화슬러지와 접촉하는 과정에 있어서도, 도 2에서와 같은 종래의 교반기(200)는 수평면 상을 회전하는 교반기(200)에 의하여 폐기물이 교반되는데, 혐기성 소화조(100)로 처리되는 폐기물은 반액, 반고상의 일종의 페이스트(paste)로서 일반 액체와 달리 교반기(200)를 극저속으로 회전시킬 수 밖에 없으며, 따라서 교반기(200) 상, 하부간의 원활한 혼합을 기대할 수 없다.In addition, even in the process of contacting the lowered waste digestion sludge under the digester 100, the conventional stirrer 200 as shown in Figure 2 is agitated by the stirrer 200 rotating on a horizontal plane, anaerobic The waste treated with the digester 100 is a semi-solid, semi-solid paste that can only rotate the stirrer 200 at a very low speed, unlike ordinary liquids. Therefore, smooth mixing between the upper and lower portions of the stirrer 200 is expected. Can not.

본 발명은 전술한 문제점을 감안하여 창안한 것으로, 상부에 덮개(120)가 설치되어 밀폐되는 소화조(100)와, 소화조(100) 벽체 상단을 포위하는 환형수로(130)와, 소화조(100) 중심부에 설치되는 입상관(140)과, 입상관(140) 내부로 처리대상 반액상 폐기물을 공급하는 유입관(111)과, 환형수로(130), 덮개(120) 및 소화조(100) 하단부에 각각 설치되는 배수관(112), 배기관(121) 및 배출관(113)으로 구성되는 혐기성 소화장치에 있어서, 입상관(140)의 내부에는 입상관(140)을 횡단하는 다수의 다공판(141)이 설치되되, 이 다공판(141)에는 다수의 통공(142)이 형성됨을 특징으로 하는 반액상 유기 폐기물 처리용 혐기성 소화장치이다.The present invention has been made in view of the above-described problems, the cover 120 is installed on the top of the digester 100 is sealed, the digester 100, the annular waterway 130 surrounding the top of the wall, and the digester 100 ) A riser pipe 140 installed at the center, an inflow pipe 111 for supplying semi-liquid waste to be processed into the riser pipe 140, an annular water channel 130, a cover 120, and a digester 100 In the anaerobic digestion apparatus composed of a drain pipe 112, an exhaust pipe 121, and an exhaust pipe 113 respectively installed at a lower end portion, a plurality of porous plates 141 crossing the granular pipe 140 inside the granular pipe 140. ) Is installed, the porous plate 141 is an anaerobic digestion apparatus for processing semi-liquid organic waste, characterized in that a plurality of through holes 142 are formed.

또한, 상부에 덮개(120)가 설치되어 밀폐되는 소화조(100)와, 소화조(100) 벽체 상단을 포위하는 환형수로(130)와, 소화조(100) 중심부에 설치되는 입상관(140)과, 입상관(140) 내부로 처리대상 반액상 폐기물을 공급하는 유입관(111)과, 환형수로(130), 덮개(120) 및 소화조(100) 하단부에 각각 설치되는 배수관(112), 배기관(121) 및 배출관(113)으로 구성되는 혐기성 소화장치에 있어서, 소화조(100) 중심부에는 구동모터(290)에 의하여 구동되는 교반축(210)이 설치되고, 소화조(100)의 하부에는 소화조(100) 내주면을 따라 교반축(210)과 동심의 주행환(205)이 설치되며, 교반축(210)의 하단에는 교반축(210)과 직교하는 횡축(201)이 설치되고, 횡축(201)에는 선단과 외주면에 각각 주행륜(204)과 다수의 교반익(203)이 형성된 중공축(202)이 회전가능하도록 결합되어, 교반축(210)이 회전하여 주행 륜(204)이 주행환(205)을 따라 공전주행함에 따라 교반익(203)이 교반축(210)을 축으로 회전함과 동시에 횡축(201)을 축으로도 회전함을 특징으로 하는 반액상 유기 폐기물 처리용 혐기성 소화장치이다.In addition, the cover 120 is installed on the top of the digester 100 is sealed, the annular waterway 130 surrounding the digester 100, the wall top, the granular pipe 140 is installed in the center of the digester 100 and , An inlet pipe 111 for supplying the semi-liquid waste to be treated into the standing pipe 140, an annular water channel 130, a cover 120, and a drain pipe 112 installed at a lower end of the digester 100, an exhaust pipe In the anaerobic digestion apparatus composed of a 121 and an exhaust pipe 113, a stirring shaft 210 driven by a driving motor 290 is installed at a center of the digester 100, and a digester ( 100) the stirring shaft 210 and the concentric running ring 205 is installed along the inner circumferential surface, the horizontal axis 201 orthogonal to the stirring shaft 210 is installed at the lower end of the stirring shaft 210, the horizontal axis 201 The hollow shaft 202 formed with a driving wheel 204 and a plurality of stirring blades 203 are rotatably coupled to the front and outer peripheral surfaces thereof, and the stirring shaft 210 rotates. As the driving wheel 204 idles along the traveling ring 205, the stirring blade 203 rotates about the axle shaft 210 and also rotates the horizontal shaft 201 about the shaft. Anaerobic digestion system for liquid organic waste treatment.

본 발명을 통하여 혐기성 소화장치의 처리효율를 제고하고, 처리용량 대비 소요 용적 및 체류시간을 감축하여 전체 혐기성 소화설비의 규모를 소형화함으로써 혐기성 소화설비의 보급을 확대하고, 소화가스의 연료화 및 퇴비 생산 등 친환경 에너지 및 자원 재생산을 활성화하는 효과를 얻을 수 있다.Through the present invention, the treatment efficiency of the anaerobic digestion system is improved, the required volume and residence time are reduced compared to the treatment capacity, and the size of the entire anaerobic digestion system is reduced, thereby expanding the spread of the anaerobic digestion system, fueling and producing compost gas, etc. The effect of activating eco-friendly energy and resource reproduction can be obtained.

본 발명의 상세한 구성 및 작동원리를 첨부된 도면을 통하여 설명하면 다음과 같다.The detailed configuration and operation principle of the present invention will be described with reference to the accompanying drawings.

우선 도 3은 본 발명의 부분절단 사시도로서, 동 도면을 통하여 알 수 있는 바와 같이, 본 발명의 소화조(100)내 입상관(140)에는 다수의 다공판(141)이 설치된다.First, Figure 3 is a partial cutaway perspective view of the present invention, as can be seen through the figure, a plurality of porous plates 141 are installed in the granular pipe 140 in the digester 100 of the present invention.

다공판(141)은 입상관(140)을 횡단하여 설치되며, 다공판(141) 내부에는 다수의 통공(142)이 형성되어 도 4에서와 같이, 입상관(140)으로 유입된 반액상 폐기물은 통공(142)을 통과하면서 하강하게 된다.The porous plate 141 is installed to cross the granular pipe 140, a plurality of through-holes 142 are formed in the porous plate 141, as shown in Figure 4, semi-liquid waste introduced into the granular pipe 140 Is lowered while passing through the through-hole 142.

이렇듯 통공(142)을 통하여 하강하는 과정에서 반액상 폐기물이 분류 및 합 류를 반복하면서 교란되므로 반액상 폐기물 구성성분의 불요(不要) 분리가 방지된다.As the semi-liquid waste is disturbed while repeating the sorting and merging in the process of descending through the through-hole 142 as described above, unnecessary separation of the semi-liquid waste components is prevented.

다공판(141)에 다수 형성되는 통공(142)은 가능한 한 조밀하게 천공하여 반액상 폐기물의 소통능력을 최대한 확보할 수 있도록 구성하며, 도 5에서와 같이, 인접한 다공판(141)의 통공(142)이 가능한 한 중첩되지 않도록, 즉 통공(142) 중심에서 인접한 다공판(141)에 내린 수선의 발이 통공(142) 내부에 위치하지 않도록 구성함으로써 다공판(141)으로 인한 교란효과를 극대화한다.A plurality of through-holes 142 formed in the porous plate 141 is constructed so as to perforate as tightly as possible to ensure the maximum communication capacity of the semi-liquid waste, and as shown in Figure 5, the through-holes of the adjacent porous plate 141 ( Maximize the disturbance effect due to the porous plate 141 by configuring so that the 142 is not overlapped as much as possible, that is, the foot of the waterline that falls from the center of the through hole 142 to the adjacent through plate 141 is not positioned inside the through hole 142. .

입상관(140)을 통과하며 하강된 반액상 폐기물은 혐기성 미생물에 의하여 분해되며, 이과정에서 메탄 등의 소화가스와 상등수가 형성되어 각각 배기관(121) 및 배수관(112)을 통하여 배출된다.The semi-liquid waste dropped through the granular pipe 140 is decomposed by anaerobic microorganisms, and in this process, digestive gas such as methane and the like are formed and discharged through the exhaust pipe 121 and the drain pipe 112, respectively.

상등수는 소화조(100) 벽체 상단을 월류하여 소화조(100) 상부 외주면을 포위하는 환형수로(130)로 유입되며 환형수로(130) 하부에 연결된 배수관(112)을 통하여 배출된다.The supernatant flows through the upper part of the wall of the digester 100 and flows into the annular channel 130 surrounding the upper peripheral surface of the digester 100 and is discharged through the drain pipe 112 connected to the lower part of the annular channel 130.

한편, 도 3 내지 도 5에서와 같이, 소화조(100)의 하부에는 교반수단으로서 횡축(201) 및 이에 결합된 중공축(202) 등이 설치된다.On the other hand, as shown in Figures 3 to 5, the lower portion of the digester 100 is provided with a horizontal axis 201 and a hollow shaft 202 coupled thereto as a stirring means.

본 발명의 교반수단은 도시된 바와 같이, 수평면상의 회전 뿐 아니라 수직면상의 회전이 동시에 이루어질 수 있도록 구성되는데, 이러한 복합회전은 수직축인 교반축(210)에 수평축인 횡축(201)이 연결되고, 이 횡축(201)에 교반익(203)이 회전가능하도록 설치됨으로써 달성된다.As shown in the present invention, the stirring means is configured such that the rotation on the vertical plane as well as the rotation on the horizontal plane can be made at the same time. This complex rotation is connected to the horizontal axis 201 on the horizontal axis to the stirring shaft 210 which is the vertical axis. This is achieved by installing the stirring blade 203 rotatably on the horizontal axis 201.

즉, 도 6 및 도 7에서와 같이, 소화조(100)의 중심에 설치되고 구동모 터(290)에 의하여 구동되는 교반축(210)의 하단에는 교반축(210)과 직교하는 횡축(201)을 설치하고, 이 횡축(201)에는 선단과 외주면에 각각 주행륜(204)과 다수의 교반익(203)이 형성된 중공축(202)을 회전가능하도록 결합하며, 소화조(100)의 하부에는 교반축(210)과 동심의 주행환(205)을 소화조(100)의 내주면을 따라 설치하여, 중공축(202)의 주행륜(204)이 주행환(205)을 따라 공전주행할 수 있도록 구성함으로써, 교반축(210)이 회전함에 따라 횡축(201)은 수평면상에서 회전하고, 교반익(203)이 형성된 중공축(202)은 수평면상에 회전함과 동시에 횡축(201)을 축으로 수직면상에서도 회전하는 것이다.That is, as shown in FIGS. 6 and 7, a horizontal axis 201 orthogonal to the stirring shaft 210 is installed at the lower end of the stirring shaft 210 installed in the center of the digester 100 and driven by the driving motor 290. The horizontal shaft 201 is rotatably coupled to the hollow shaft 202, the driving wheel 204 and the plurality of stirring blades 203 formed on the front and outer peripheral surfaces, respectively, and the lower portion of the digester 100 is stirred. The driving ring 205 concentric with the shaft 210 is installed along the inner circumferential surface of the digester 100 so that the driving wheel 204 of the hollow shaft 202 can idle along the traveling ring 205. As the stirring shaft 210 rotates, the horizontal axis 201 rotates on the horizontal plane, and the hollow shaft 202 on which the stirring blade 203 is formed rotates on the horizontal plane and also on the vertical plane around the horizontal axis 201. It is.

이로써, 수평면상의 회전만이 이루어지는 종래의 교반수단에 비하여 월등히 향상된 교반효과를 얻을 수 있으며, 교반대상물이 반액상이므로 극저속 회전만이 가능함을 감안할 때, 수평면 및 수직면 상의 복합회전을 통한 교반성능 제고는 분해효율 향상에도 크게 기여할 수 있다.As a result, a much improved stirring effect can be obtained as compared to the conventional stirring means which only rotates on the horizontal plane, and since the stirring object is half-liquid, it is possible to use only a very low speed rotation, thereby improving the stirring performance through the combined rotation on the horizontal plane and the vertical plane. Can greatly contribute to the improvement of decomposition efficiency.

한편 도시된 바와 같이, 주행륜(204)과 주행환(205)에는 서로 치합되는 치열을 각각 형성하여 반액상 폐기물로 인한 주행륜(204) 및 주행환 간의 윤활작용을 방지하고 안정적인 작동이 가능하도록 하는 것이 바람직하다.On the other hand, as shown in the running wheels 204 and the driving ring 205 to form the teeth that are engaged with each other to prevent lubrication between the driving wheel 204 and the driving ring due to the semi-liquid waste to enable a stable operation It is desirable to.

도 1은 혐기성 소화시설 예시도1 is an illustration of anaerobic digestion facilities

도 2는 종래의 혐기성 소화장치 대표단면도Figure 2 is a representative cross-sectional view of a conventional anaerobic digester

도 3은 본 발명의 부분절단 사시도3 is a partial cutaway perspective view of the present invention

도 4는 본 발명의 작동상태 대표단면도Figure 4 is a representative cross-sectional view of the operating state of the present invention

도 5는 본 발명의 입상관 및 다공판 상세도Figure 5 is a detailed view of the granular pipe and the porous plate of the present invention

도 6은 본 발명의 교반기 요부 발췌 사시도Figure 6 is a perspective view of the main portion of the stirrer extract of the present invention

도 7은 본 발명의 중공축 부분절단 사시도Figure 7 is a hollow shaft partial cutaway perspective view of the present invention

<도면의 주요부분에 대한 부호설명><Code Description of Main Parts of Drawing>

100 : 소화조100: digester

111 : 유입관111: inlet pipe

112 : 배수관112: drain pipe

113 : 배출관113: discharge pipe

120 : 덮개120: cover

121 : 배기관121: exhaust pipe

130 : 환형수로130: annular waterway

140 : 입상관140: winning a prize

141 : 다공판141: perforated plate

142 : 통공142: through

200 : 교반기200: Stirrer

201 : 횡축201: horizontal axis

202 : 중공축202: hollow shaft

203 : 교반익203: stirring blade

204 : 주행륜204: driving wheel

205 : 주행환205: driving ring

210 : 교반축210: stirring shaft

290 : 구동모터290: drive motor

Claims (2)

상부에 덮개(120)가 설치되어 밀폐되는 소화조(100)와, 소화조(100) 벽체 상단을 포위하는 환형수로(130)와, 소화조(100) 중심부에 설치되는 입상관(140)과, 입상관(140) 내부로 처리대상 반액상 폐기물을 공급하는 유입관(111)과, 환형수로(130), 덮개(120) 및 소화조(100) 하단부에 각각 설치되는 배수관(112), 배기관(121) 및 배출관(113)으로 구성되는 혐기성 소화장치에 있어서,Digestion tank 100, the cover 120 is installed on the upper part, the annular waterway 130 surrounding the upper wall of the digester 100, the granular pipe 140 is installed in the center of the digester 100, mouth An inlet pipe 111 for supplying the semi-liquid waste to be treated into the boss 140, an annular water channel 130, a cover 120, and a drain pipe 112 and an exhaust pipe 121 installed at a lower end of the digester 100, respectively. In the anaerobic digestion apparatus consisting of a) and the discharge pipe 113, 입상관(140)의 내부에는 입상관(140)을 횡단하는 다수의 다공판(141)이 설치되되, 이 다공판(141)에는 다수의 통공(142)이 형성됨을 특징으로 하는 반액상 유기 폐기물 처리용 혐기성 소화장치.Semi-liquid organic waste, characterized in that a plurality of perforated plate 141 traversing the riser tube 140 is installed inside the granular tube 140, the plurality of through-holes 142 are formed in the porous plate 141. Anaerobic digester for treatment. 상부에 덮개(120)가 설치되어 밀폐되는 소화조(100)와, 소화조(100) 벽체 상단을 포위하는 환형수로(130)와, 소화조(100) 중심부에 설치되는 입상관(140)과, 입상관(140) 내부로 처리대상 반액상 폐기물을 공급하는 유입관(111)과, 환형수로(130), 덮개(120) 및 소화조(100) 하단부에 각각 설치되는 배수관(112), 배기관(121) 및 배출관(113)으로 구성되는 혐기성 소화장치에 있어서,Digestion tank 100, the cover 120 is installed on the upper part, the annular waterway 130 surrounding the upper wall of the digester 100, the granular pipe 140 is installed in the center of the digester 100, mouth An inlet pipe 111 for supplying the semi-liquid waste to be treated into the boss 140, an annular water channel 130, a cover 120, and a drain pipe 112 and an exhaust pipe 121 installed at a lower end of the digester 100, respectively. In the anaerobic digestion apparatus consisting of a) and the discharge pipe 113, 소화조(100) 중심부에는 구동모터(290)에 의하여 구동되는 교반축(210)이 설치되고;A stirring shaft 210 driven by the driving motor 290 is installed at the center of the digester 100; 소화조(100)의 하부에는 소화조(100) 내주면을 따라 교반축(210)과 동심의 주행환(205)이 설치되며;A lower portion of the digester 100 is provided with a stirring shaft 210 and a concentric running ring 205 along the inner circumferential surface of the digester 100; 교반축(210)의 하단에는 교반축(210)과 직교하는 횡축(201)이 설치되고;A horizontal shaft 201 orthogonal to the stirring shaft 210 is installed at the lower end of the stirring shaft 210; 횡축(201)에는 선단과 외주면에 각각 주행륜(204)과 다수의 교반익(203)이 형성된 중공축(202)이 회전가능하도록 결합되어, 교반축(210)이 회전하여 주행륜(204)이 주행환(205)을 따라 공전주행함에 따라 교반익(203)이 교반축(210)을 축으로 회전함과 동시에 횡축(201)을 축으로도 회전함을 특징으로 하는 반액상 유기 폐기물 처리용 혐기성 소화장치.The horizontal shaft 201 is rotatably coupled to the hollow shaft 202 having the driving wheel 204 and the plurality of stirring blades 203 formed on the front and outer circumferential surfaces thereof, respectively, such that the stirring shaft 210 rotates to the driving wheel 204. As the idler blade 203 rotates along the traveling ring 205, the stirring blade 203 rotates about the axis of the stirring shaft 210 and also rotates about the axis of the horizontal axis 201. Anaerobic digestive system.
KR20080015913A 2008-02-21 2008-02-21 Anaerobic digestion apparatus for semi-liquid organic waste treatment KR100836149B1 (en)

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US5942116A (en) 1997-08-01 1999-08-24 Clark; Sidney E. Anaerobic sludge digester
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