KR20000033369A - Organic trash disposer - Google Patents
Organic trash disposer Download PDFInfo
- Publication number
- KR20000033369A KR20000033369A KR1019980050209A KR19980050209A KR20000033369A KR 20000033369 A KR20000033369 A KR 20000033369A KR 1019980050209 A KR1019980050209 A KR 1019980050209A KR 19980050209 A KR19980050209 A KR 19980050209A KR 20000033369 A KR20000033369 A KR 20000033369A
- Authority
- KR
- South Korea
- Prior art keywords
- organic waste
- heating tube
- organic
- discharge
- refuse
- Prior art date
Links
- 239000010813 municipal solid waste Substances 0.000 title abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 31
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000010815 organic waste Substances 0.000 claims description 60
- 238000007906 compression Methods 0.000 claims description 27
- 230000006835 compression Effects 0.000 claims description 26
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims 1
- 239000002361 compost Substances 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 150000003839 salts Chemical class 0.000 abstract description 3
- 230000001174 ascending effect Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 239000010794 food waste Substances 0.000 description 8
- 238000000855 fermentation Methods 0.000 description 7
- 230000004151 fermentation Effects 0.000 description 7
- 208000005156 Dehydration Diseases 0.000 description 5
- 230000018044 dehydration Effects 0.000 description 5
- 238000006297 dehydration reaction Methods 0.000 description 5
- 244000144972 livestock Species 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 239000010871 livestock manure Substances 0.000 description 3
- -1 and in particular Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000010828 animal waste Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000012840 feeding operation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000013024 troubleshooting Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/10—Animal feeding-stuffs obtained by microbiological or biochemical processes
- A23K10/12—Animal feeding-stuffs obtained by microbiological or biochemical processes by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B1/00—Dumping solid waste
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2200/00—Waste incineration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
본 발명은 유기물쓰레기를 처리하는 장치에 관한 것으로, 특히 유기물쓰레기 즉, 음식물 쓰레기, 가축분뇨, 오니 등과 같은 유기물을 고온고압으로 가열한 후 폭발시키듯 토출시켜 수분을 기화 및 증발시키므로써 건조시켜 가축사료나 퇴비로 사용하도록 하거나 소각 또는 매립처리할 수 있도록 장치에 관한 것이다.The present invention relates to an apparatus for processing organic waste, and in particular, organic waste, that is, organic matter such as food waste, livestock manure, sludge, etc., heated to a high temperature and high pressure, and then discharged as if exploded to evaporate and evaporate moisture to dry livestock Apparatus for use as feed or compost, for incineration or landfill.
일반적으로 음식물쓰레기나 가축배설물이나, 정수장과 같은 곳에서 식수를 얻기 위해 정수시킬 때 또는 하수종말처리장에서 하수처리를 할 때 부산물로 발생하는 곤죽상태의 오니(이하 유기물쓰레기라 함) 등을 처리하는 방법에는 매립 또는 소각시키는 방법 그리고 발효장치로 발효시켜 퇴비 또는 가축의 사료로 재활용하는 방법 등이 있다.In general, it is used to treat sludge (hereinafter referred to as organic waste) generated as a by-product when water is purified to obtain drinking water at food wastes, animal wastes, or water purification plants or when sewage treatment is performed at sewage treatment plants. Methods include landfill or incineration, fermentation by fermentation, and recycling into compost or livestock feed.
이와 같이 처리하기 위해서는 유기물쓰레기의 수분을 탈수시켜야 한다. 탈수처리방법에는 원심탈수 및 압착탈수 등이 있는데, 곤죽상태의 유기물쓰레기를 원심 및 압착탈수시키게 되면 수분을 비롯하여 입자가 작은 음식물쓰레기가 함께 빠져나가기 때문에 2차공해를 유발하게 되는 폐단을 낳게 되는 폐단이 있다.This treatment requires dehydration of the organic waste. Dehydration treatment methods include centrifugal dehydration and compressed dehydration. When decontamination and compression dehydration of contaminated organic waste are produced, wastes that cause secondary pollution are caused by food waste with small particles. There is this.
또 발효건조시켜 퇴비나 가축사료로 사용하는 방법은 발효처리 장치의 부피가 크고 발효에 필요한 적당한 온도를 유지시켜주어야만 발효 효율이 높아져 양질의 사료를 얻을 수 있고, 또 온도를 적당하게 유지시키게 되면 발효시간이 길어져 연료의 소모량이 많아지므로 결국 유기물쓰레기의 처리용량이 떨어지고 엄청난 장비운영비용이 소요되는 폐단이 있었다.In addition, fermentation drying method used as compost or livestock feed should be maintained only when the volume of fermentation system is large and maintain the proper temperature required for fermentation to increase fermentation efficiency to obtain high quality feed, and fermentation when temperature is maintained properly As time goes by and fuel consumption increases, the disposal capacity of organic waste falls down and enormous equipment operation costs are required.
따라서 본 발명은 이러한 종래의 폐단을 해소하기 위해 창안한 것으로서, 그 목적은 유압펌프를 이용하여 고압으로 압송시키면서 열을 가한 후 토출구로 고속으로 토출시킴과 동시에 건조시켜 가축의 사료 또는 퇴비로 사용하거나 소각 및 매립처리토록 하므로써 다량의 유기물 쓰레기를 공해없이 저렴한 비용으로 신속 간편하게 처리할 수 있는 유기물쓰레기 처리장치를 제공하는데 있다.Therefore, the present invention was devised to solve such a conventional waste end, the purpose of which is to use a hydraulic pump to feed at high pressure while being discharged at high speed and discharged at the same time to the discharge port and dried to use as feed or compost of livestock or By incineration and landfill treatment, it is to provide an organic waste treatment apparatus that can quickly and easily treat a large amount of organic waste without pollution.
도 1은 본 발명의 유기물쓰레기 처리장치의 구조를 나타낸 종단면도,1 is a longitudinal sectional view showing the structure of the organic waste treatment apparatus of the present invention;
도 2는 본 발명의 유기물쓰레기 처리장치의 구조를 나타낸 측단면도,Figure 2 is a side cross-sectional view showing the structure of the organic waste treatment apparatus of the present invention,
*** 도면의 주요 부분에 대한 부호의 설명 ****** Explanation of symbols for the main parts of the drawing ***
10 - 압축가열통 11 - 지지틀 12 - 히터장치10-Compression Heater 11-Support Frame 12-Heater
13 - 단열벽 14 - 노즐 15 - 온도센서13-Insulation Wall 14-Nozzle 15-Temperature Sensor
16 - 토출판 17 - 토출구 18 - 볼트16-discharge plate 17-discharge port 18-bolt
19 - 분산봉 20 - 망체 22 - 배기통19-Scatter bar 20-Mesh 22-Exhaust box
24 - 배출슈트 26 - 버큠펌프 28 - 그릴24-Discharge chute 26-Blow pump 28-Grill
30 - 호퍼 32 - 펌프장치 33a,33b - 실린더30-Hopper 32-Pump Unit 33a, 33b-Cylinder
34a,34b - 피스톤 35a,35b - 유압실린더 36 - 공급관34a, 34b-Piston 35a, 35b-Hydraulic Cylinder 36-Supply Line
37 - 모터 38 - 체인 40 - 이송컨베이어37-motor 38-chain 40-conveyor
42 - 공급호퍼42-feed hopper
상기 목적을 달성하기 위한 본 발명의 유기물쓰레기 처리장치는, 유기물쓰레기가 투입되는 호퍼와;Organic waste treatment apparatus of the present invention for achieving the above object, and a hopper to which the organic waste is put;
상기 호퍼의 하부와 연결되어 유기물쓰레기를 압송받아 열을 가하여 건조시키면서 토출시키는 압축가열통과;A compression heating passage connected to a lower portion of the hopper to discharge the organic wastes by applying heat and drying them;
상기 호퍼의 하부에 설치되어 유기물쓰레기를 압축가열통으로 압송하는 펌프수단과;A pump means installed at a lower portion of the hopper to pump organic waste into a compression heating tube;
상기 압축가열통의 상부에 설치되어 토출된 유기물쓰레기를 임시 저장하고, 저장된 유기물쓰레기를 배출시킴과 동시에 상부에 설치된 배기통으로 습기 및 가스를 배출시키는 망체들로 구성되어 달성된다.It is achieved by consisting of nets installed in the upper part of the compression heating cylinder to temporarily store the discharged organic waste, discharge the stored organic waste and at the same time to discharge the moisture and gas to the exhaust pipe installed in the upper portion.
이하, 본 발명의 실시예를 첨부된 도면을 참조하여 상세히 설명한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명의 유기물쓰레기 처리장치의 구조를 나타낸 종단면도이고, 도 2는 본 발명의 유기물쓰레기 처리장치의 구조를 나타낸 측단면도이다.1 is a longitudinal cross-sectional view showing the structure of the organic waste treatment apparatus of the present invention, Figure 2 is a side cross-sectional view showing the structure of the organic waste treatment apparatus of the present invention.
도시된 바와 같이 압축가열통(10)은 원통형으로 형성되어 하부에 지지틀(11)에 의해 수직으로 설치되어 있다. 압축가열통(10)의 상하부를 제외한 둘레에는 내부를 대략 300∼500℃로 가열하는 히터장치(12)가 설치되어 있으며, 압축가열통(10)의 둘레에는 단열벽(13)이 둘러싸여 압축가열통(10)의 내부온도를 보온하도록 되어 있다. 압축가열통(10)의 중앙부 둘레에는 상향된 노즐(14)이 형성되어 도면에 도시되지 않은 산소탱크로부터 액체 또는 기체 산소를 내부로 공급시킬 수 있도록 되어 있으며, 상하부에는 다수개의 온도센서(15)들이 설치되어 압축가열통(10)의 각부위에 따른 온도를 체킹하여 각 부분마다 적당한 온도를 유지할 수 있도록되어 있다. 또한 압축가열통(10)의 상부에는 토출판(16)이 결합되어 있다. 이 토출판(16)은 둘레에 상광하협된 형상으로 상하 관통된 다수개의 토출구(17)가 형성되어 있고 그 중앙하부에는 하단이 비교적 뾰족하게 형성되어 압송되는 유기물쓰레기를 외부로 분산시키는 분산봉(19)이 형성되어 있다. 그리고 토출판(16)의 토출구(17) 및 압축가열통(10)의 내부 점검이나 고장수리 및 청소를 용이하게 수행할 수 있도록 하기 위해 볼트(18)로 분해조립이 용이토록 되어 있다.As shown, the compression heating tube 10 is formed in a cylindrical shape and is vertically installed by the support frame 11 at the bottom. A heater device 12 for heating the interior to approximately 300 to 500 ° C. is installed on the periphery of the compression heating tube 10 except for the upper and lower parts thereof. The heat insulation wall 13 is surrounded by the compression heating tube 10 to compress the heating. The internal temperature of the cylinder 10 is kept warm. An upward nozzle 14 is formed around the central portion of the compression heating tube 10 to supply liquid or gaseous oxygen from an oxygen tank not shown in the drawing, and a plurality of temperature sensors 15 are provided on the upper and lower portions thereof. They are installed to check the temperature according to each part of the compression heating tube 10 to maintain the appropriate temperature for each part. In addition, the discharge plate 16 is coupled to the upper portion of the compression heating tube (10). The discharge plate 16 is formed with a plurality of discharge holes 17 penetrating up and down in the shape of the upper and lower narrow circumference, the lower end of the discharge plate 16 is formed with a relatively sharp bottom end to disperse the transported organic waste to the outside ( 19) is formed. And disassembly and assembly of the bolt 18 to facilitate the internal inspection, troubleshooting and cleaning of the discharge port 17 and the compression heating tube 10 of the discharge plate 16 is easy.
또한 압축가열통(10)의 상부에 설치된 망체(20)는 유기물쓰레기를 임시 저장할 수 있도록 넓은 내부공간을 가지고 있으며 상부에는 유기물쓰레기의 건조시 발생하는 습기 및 가스를 배출시키는 배기통(22)이 설치되어 있고 측면부에는 임시 저장된 유기물쓰레기를 하부로 배출시키는 배출슈트(24)가 설치되어 있다. 특히 배기통(22)은 버큠펌프(26)에 의해 공기를 강제 흡입하도록 되어 있고, 배기통(22)의 하부에는 토출된 유기물쓰레기가 배기통(22)으로 빨려들어가지 않도록 그릴(28)이 형성되어 있다. 또 이러한 망체(20)는 지지프레임에 의해 수평 회동가능하게 설치되어 있다.In addition, the mesh 20 installed in the upper portion of the compression heating tube 10 has a large internal space for temporarily storing the organic waste, and the exhaust pipe 22 for discharging moisture and gas generated during drying of the organic waste is installed in the upper portion. The side part is provided with a discharge chute 24 for discharging the temporarily stored organic waste to the bottom. In particular, the exhaust cylinder 22 is forced to suck air by the pump pump 26, the grill 28 is formed in the lower portion of the exhaust cylinder 22 so that the discharged organic waste is not sucked into the exhaust cylinder (22). . In addition, the mesh 20 is installed to be horizontally rotated by the support frame.
압축가열통(10)의 측부에 설치된 호퍼(30)의 하부에는 유기물쓰레기를 압축가열통(10)으로 압송하는 펌프장치(32)가 설치되어 있다. 펌프장치(32)는 몰타르상태의 콘크리트를 압송하는 다양한 구조의 공지의 펌프장치를 적용하는 것으로서, 도 2에서 도시한 바와 같이 양측에 두 개의 실린더(33a)(33b)를 구비하고, 이 두실린더(33a)(33b)에는 실린더(33a)(33b)를 왕복운동하는 피스톤(34a)(34b)이 설치되어 있으며, 이 피스톤(34a)(34b)은 교호로 출몰작동하는 유압실린더(35a)(35b)에 의해 작동된다. 참조번호 35는 유압펌프이다.In the lower part of the hopper 30 provided in the side part of the compression heating tube 10, the pump apparatus 32 which delivers organic waste to the compression heating cylinder 10 is provided. The pump device 32 applies a well-known pump device of various structures for pumping concrete in a mortar state, and has two cylinders 33a and 33b on both sides, as shown in FIG. Pistons 34a and 34b for reciprocating the cylinders 33a and 33b are provided at (33a) and (33b), and the pistons (34a) and (34b) are hydraulic cylinders (35a) which are alternately indented and operated. 35b). Reference numeral 35 is a hydraulic pump.
그리고 실린더(33a)(33b)의 선단부에는 유기물쓰레기를 압축가열통(10)으로 공급하는 공급관(36)이 설치되어 있다. 이 공급관(36)은 압축가열통(10)과 호퍼(30)의 하부에서 회동되는 구조로 설치되어 있으며, 양측실린더(33a)(33b)의 선단부사이를 피스톤(34a)(34b)의 동작에 연동하여 유동한다. 이와 같은 동작은 양측 두 피스톤(34a)(34b)의 동작에 연동하는 스위치작동에 의해 정역회전하는 모터(37)와 체인(38)으로 연결되어 작동하게 된다.At the distal end of the cylinders 33a and 33b, a supply pipe 36 for supplying the organic waste to the compression heating tube 10 is provided. The supply pipe 36 is installed in a structure that is rotated in the lower portion of the compression heating tube 10 and the hopper 30, and the operation of the piston 34a (34b) between the front end portions of both cylinders (33a) (33b). Flow in conjunction. Such an operation is connected to the motor 37 and the chain 38, which is rotated forward and backward, by a switch operation in conjunction with the operation of both pistons 34a and 34b.
또한 호퍼(30)의 상부 일측에는 유기물쓰레기를 이송공급하는 컨베이어(40)가 설치되어 있으며, 이송컨베이어(40)의 일측단 상부에는 유기물쓰레기를 공급하는 공급호퍼(42)가 설치되어 있다.In addition, a conveyor 40 for transporting and supplying organic waste is installed at one upper side of the hopper 30, and a supply hopper 42 for supplying organic waste is installed at one upper end of the transport conveyor 40.
이러한 구성에 의한 본 발명의 작동관계를 살펴보면 다음과 같다.Looking at the operation of the present invention by this configuration as follows.
본 발명의 유기물쓰레기장치는 음식물쓰레기, 가축분뇨 또는 각종 오니 등의 유기물쓰레기를 공급호퍼(42)에 투입시키면 이송컨베이어(40)에 의해 이송되어 호퍼(30)로 투입된다. 투입된 음식물쓰레기는 유압에 의해 실린더(33a)(33b)내에서 교호로 진퇴작동하는 피스톤(34a)(34b)이 유기물쓰레기를 압축가열통(10)으로 압송하게 된다. 이를 좀더 상세히 설명하면, 일측 피스톤(34a)(34b)이 후퇴하면 타측 피스톤(34a)(34b)은 전진하게 되어 후퇴할 때는 호퍼(30)내의 유기물쓰레기를 흡입하게 되고, 전진할 때는 흡입된 유기물쓰레기를 압송하는 동작을 반복하게 된다. 이와 동시에 공급관(36)은 피스톤(34a)(34b)의 동작에 의해 작동하는 모터(37)에 의해 일측피스톤(34a)(34b)이 흡입하게 되면 신속하게 회동하여 피스톤(34a)(34b)이 전진하는 실린더(33a)(33b)의 입구부와 연결되고, 다시 전진한 피스톤(34a)(34b)이 후퇴하게 되고 후퇴해 있던 피스톤(34a)(34b)이 전진하게 되면 공급관(36)은 신속하게 회동하여 전진하는 피스톤(34a)(34b)의 실린더(33a)(33b) 입구에 연결된다. 이때 피스톤(34a)(34b)이 흡입행정에 있는 실린더(33a)(33b)의 입구는 호퍼(30)내에서 노출되기 때문에 호퍼(30)내의 유기물쓰레기가 실린더(33a)(33b)의 내부로 흡입되게 되고, 피스톤(34a)(34b)의 전진시 공급관(36)을 통해 유기물쓰레기를 압축가열통(10)에 압송시키게 된다. 이러한 압송동작은 연속적으로 이루어진다.In the organic trash device of the present invention, when organic trash such as food waste, livestock manure or various sludge is put into the feed hopper 42, the organic trash is conveyed by the transfer conveyor 40 and is introduced into the hopper 30. The injected food waste is hydraulically pushed back and forth by the pistons 34a and 34b in the cylinders 33a and 33b to pressurize the organic waste into the compression heating tube 10. In more detail, when one side piston (34a) (34b) is retracted, the other side piston (34a) (34b) is advancing, and when retreating to suck the organic waste in the hopper 30, and when advancing the sucked organic matter The operation of transporting garbage is repeated. At the same time, the supply pipe 36 is rapidly rotated when the one side pistons 34a and 34b are sucked by the motor 37 operated by the operation of the pistons 34a and 34b. When the pistons 34a and 34b which are advanced are retracted and the pistons 34a and 34b which have been retracted are advanced, the supply pipe 36 is rapidly It is connected to the inlets of the cylinders 33a and 33b of the pistons 34a and 34b which rotate and move forward. At this time, since the inlets of the cylinders 33a and 33b in which the pistons 34a and 34b are in the intake stroke are exposed in the hopper 30, the organic waste in the hopper 30 enters the cylinders 33a and 33b. When the pistons 34a and 34b are advanced, the organic waste is fed to the compression heating tube 10 through the supply pipe 36. This feeding operation is performed continuously.
연속적으로 압송되는 유기물쓰레기는 압축가열통(10)의 상부로 압송되어 압축되고, 둘레에 설치된 히터장치(12)에 의해 가열되며, 중앙부에 설치된 노즐(14)을 통해 산소를 공급받아 유기물을 산화분해(CO2와 H2O로 분해)하게 된다. 특히 히터장치(12)에 의해 가열될 때 각부분에 설치된 온도센서(15)에 의해 온도가 체킹되므로 도면에 도시되지 않은 제어부에 의해 최적온도로 가열시킬 수 있다. 이와 같이 압축이송되는 유기물쓰레기는 토출판(16)에 설치된 토출구(17)를 통해 지속적으로 토출되게 되는데, 토출구(17)를 향해 압송되는 과정에서 분산봉(19)에 의해 압축가열통(10)의 상단 내주면 쪽으로 분산되게 되어 압송되는 유기물쓰레기가 고른 온도분포로 가열되어지며 또 공간이 협소해짐에따라 압력이 더욱더 높아지게 된다.Continuously transported organic waste is compressed and compressed to the upper portion of the compression heating tube 10, is heated by the heater device 12 is installed around the oxidized organic matter by receiving oxygen through the nozzle 14 installed in the center Decomposition (CO 2 and H 2 O). In particular, since the temperature is checked by the temperature sensor 15 installed in each part when heated by the heater device 12 it can be heated to the optimum temperature by a control unit not shown in the figure. The organic waste that is compressed and transported as described above is continuously discharged through the discharge holes 17 installed in the discharge plate 16, and the compression heating tube 10 is discharged by the dispersing rod 19 in the process of being pushed toward the discharge holes 17. Dispersed toward the upper inner circumferential surface of the organic waste is heated to an even temperature distribution and the pressure becomes higher as the space becomes narrower.
이러한 상태로 유기물쓰레기가 토출판(16)까지 상승하게 되면 토출판(16)의 토출구(17)를 통해 빠른 속도로 폭발하듯이 토출되게 된다. 이때 고압상태의 압축가열통(10)내에서 갑자기 저압상태의 상부통으로 토출되기 때문에 순간적으로 튀어올러가게 되면서 부풀려지게 됨과 동시에 유기물쓰레기에 함유된 수분은 고압상태에서 갑자기 저압상태로 되기 때문에 기화작용이 신속하게 발생되어 유기물쓰레기와 분리되게 되며 기화작용에 따른 수분의 분리시 음식물에 함유된 염분도 함께 분리된다.In this state, when the organic matter rises to the discharge plate 16, it is discharged as if it explodes at a high speed through the discharge port 17 of the discharge plate 16. At this time, since it is suddenly discharged into the upper cylinder of the low pressure state in the compressed heating cylinder 10 under high pressure state, it is swelled and swelled at the same time, and at the same time, the moisture contained in the organic waste suddenly becomes low pressure under the high pressure state. It is rapidly generated and separated from organic waste, and salts contained in food are also separated when water is separated by vaporization.
유기물쓰레기는 토출구(17)를 통해 튀어올라가 망체(20)내에 모아지게 되고, 이는 곧 배출슈트(24)를 통해 배출된다. 그리고 유기물쓰레기가 토출구(17)로 토출되면서 발생된 가스 및 수분은 망체(20)의 상부에 버큠펌프(26)로 연결된 배기통(22)을 통해 신속하게 배출된다.The organic waste is thrown up through the discharge port 17 and collected in the mesh 20, which is soon discharged through the discharge chute 24. In addition, the gas and water generated while the organic waste is discharged to the discharge port 17 are quickly discharged through the exhaust pipe 22 connected to the upper pump 26 by the vacuum pump 26.
한편, 본 발명의 유기물쓰레기장치는 음식물쓰레기, 가축분뇨 또는 각종 오니 등의 유기물쓰레기를 처리할 수 있도록 한 것이나 가장 효과적으로 처리하기 위해서는 음식물쓰레기와 오니는 별도로 처리하는 것이 좋다.On the other hand, the organic waste device of the present invention is to be able to treat organic waste, such as food waste, livestock manure or various sludge, but to treat most effectively, it is preferable to treat food waste and sludge separately.
특히 음식물쓰레기를 처리할 때에는 별도의 선별기를 통하여 각종 이물질을 걸러내는 공정을 수행하도록 해야 할 뿐만 아니라 입자가 큰 음식물의 경우에는 분쇄기를 통하여 잘게 분쇄시킨 후 투입시켜야 한다.In particular, when processing food waste, not only to carry out the process of filtering out various foreign matters through a separate sorting machine, but also in the case of food having a large particle, it must be pulverized finely through a grinder and then added.
또 이와 같이 건조된 유기물쓰레기는 매립 또는 소각처리하거나 가축사료 또는 퇴비로 사용할 수 있으나, 가장 신속하고 확실하면서 적은 비용으로 공해없이 처리하는 방법은 소각처리하는 것이며, 두 번째는 완전건조된 상태이기 때문에 매립시키는 방법이 좋다.The organic waste thus dried can be landfilled or incinerated, or used as livestock feed or compost.However, the fastest, most reliable and least cost-free disposal is incineration, and the second is completely dry. Landfill is good.
이상에서 살펴본 바와 같이 본 발명은 고압펌프에 의해 유기물쓰레기가 압축가열통의 상부로 압송되면서 히터장치에 의해 고압상태에서 살균되면서 토출판의 토출구로 순간 토출됨에 따라 유기물쓰레기에 함유된 수분 및 염분이 신속하게 분리가 되어 건조되기 때문에 양질의 사료 및 퇴비를 생산할 수 있는 장점이 있다.As described above, in the present invention, water and salt contained in the organic waste are contained in the organic waste as it is discharged to the discharge port of the discharge plate while being sterilized under high pressure by the heater device while the organic waste is pumped to the upper portion of the compression heating tank by the high pressure pump. Since it is quickly separated and dried, there is an advantage in producing a good feed and compost.
또한 건조된 유기물쓰레기를 그대로 퇴비로 사용할 수 있으며, 수분이 완전히 제거된 상태이기 때문에 소각시키거나 매립을 하여도 2차공해가 발생하지 않는 장점이 있다. 특히 구조가 간단하고 소형임에도 불구하고 신속하고 효율적으로 많은 양의 유기물쓰레기를 공해없이 저렴한 비용에 처리할 수 있는 유용한 고안다.In addition, the dried organic waste can be used as a compost as it is, since the water is completely removed, there is an advantage that secondary pollution does not occur even if incinerated or landfilled. In particular, although the structure is simple and small, it is a useful design that can quickly and efficiently treat a large amount of organic waste at low cost without pollution.
Claims (7)
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| KR1019980050209A KR100281000B1 (en) | 1998-11-23 | 1998-11-23 | Organic Waste Disposal Device |
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| KR20020051915A (en) * | 2002-06-11 | 2002-06-29 | 주식회사 새재환경 | Construction wastes force injection device of crusher |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20020051915A (en) * | 2002-06-11 | 2002-06-29 | 주식회사 새재환경 | Construction wastes force injection device of crusher |
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