KR970006918B1 - Apparatus for disposal of waste matter - Google Patents
Apparatus for disposal of waste matter Download PDFInfo
- Publication number
- KR970006918B1 KR970006918B1 KR1019930028788A KR930028788A KR970006918B1 KR 970006918 B1 KR970006918 B1 KR 970006918B1 KR 1019930028788 A KR1019930028788 A KR 1019930028788A KR 930028788 A KR930028788 A KR 930028788A KR 970006918 B1 KR970006918 B1 KR 970006918B1
- Authority
- KR
- South Korea
- Prior art keywords
- tank
- waste
- combustion chamber
- methane gas
- water
- Prior art date
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 39
- 238000002485 combustion reaction Methods 0.000 claims abstract description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000002341 toxic gas Substances 0.000 claims abstract description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 17
- 238000002347 injection Methods 0.000 claims description 9
- 239000007924 injection Substances 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 239000002351 wastewater Substances 0.000 claims description 7
- 239000002361 compost Substances 0.000 claims description 5
- 238000005189 flocculation Methods 0.000 claims description 2
- 230000016615 flocculation Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 6
- 239000010849 combustible waste Substances 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 3
- 239000010812 mixed waste Substances 0.000 abstract description 2
- 239000011343 solid material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 14
- 239000010794 food waste Substances 0.000 description 7
- 239000003895 organic fertilizer Substances 0.000 description 5
- 239000003337 fertilizer Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000010791 domestic waste Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 241000442425 Aristeomorpha foliacea Species 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 240000000218 Cannabis sativa Species 0.000 description 1
- 206010037844 Rash Diseases 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000004069 differentiation Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- VTLYFUHAOXGGBS-UHFFFAOYSA-N fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/16—Treatment of sludge; Devices therefor by de-watering, drying or thickening using drying or composting beds
-
- 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
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
Abstract
Description
제1도는 본 발명의 장치 개요도1 is a schematic view of the apparatus of the present invention
제2도는 제1도 A부분의 확대 사시도2 is an enlarged perspective view of part A of FIG.
제3도는 제1도 B부분의 확대도3 is an enlarged view of part B of FIG. 1
제4도는 제1도 C부분의 확대도4 is an enlarged view of part C of FIG.
제5도는 제1도 D부분의 확대도5 is an enlarged view of part D of FIG.
*도면의 주요부분에 태한 부호의 설명* Explanation of symbols on the main parts of the drawings
1 : 제1연소실 1' : 호퍼(쓰레기 투입)1: 1st combustion chamber 1 ': hopper (trash input)
1 : 스크류 2 : 제2연소실1 screw 2 second combustion chamber
2' : 연통관 3 : 불판2 ': communication tube 3: fire plate
4, 4' : 노즐 5 :수관4, 4 ': nozzle 5: water pipe
6 : 송풍관 7 : 내화벽6: blower pipe 7: fireproof wall
8 : 폐유재생기 8' : 기름탱크8: waste oil regenerator 8 ': oil tank
8 : 분화관 8' :폐유기화 분리실8: Eruption pipe 8 ': Waste organication separation chamber
9 : 고형물연소실 9' : 통공9: solid combustion chamber 9 ': through hole
9 : 분사구(고형물 기화 가스) 9' : 개폐문9: injection hole (solid vaporization gas) 9 ': opening and closing door
10 : 메탄가스분사구 11 : 정유냉각탑10: methane gas injection hole 11: refinery cooling tower
11' : 배출관(기화) 12 : 열병합보일러11 ': discharge pipe (vaporization) 12: cogeneration boiler
13 : 사이크로톤 멀티 14, 14' : 송풍팬13: Cyctone Multi 14, 14 ': Blowing fan
15 : 물파쇄기 16 : 습식냉각장치기15: water shredder 16: wet cooling device
16' : 분수구 17 : 화학반응조16 ': fountain 17: chemical reaction tank
18 : 배기팬 19 : 유해가스 정화제18: exhaust fan 19: harmful gas purifier
19' : 오염제 소재실 19 : 망판19 ': pollutant material chamber 19: halftone
20 : 난파유동처리기 20' : 연통부(수용액)20: Wrecked flow processor 20 ': Communication part (aqueous solution)
21 : 모타 22 : 모타펌프21: motor 22: motor pump
23 : 비료가공조 24 : 메탄가스생성조23: fertilizer processing tank 24: methane gas production tank
25 : 오니 처리조 25' : 농축실25: sludge treatment tank 25 ': concentration chamber
25 :응집실 25' : 침전실25: flocculation chamber 25 ': precipitation chamber
26 : 폐수조 26': 여과정수조26: waste water tank 26 ': filtration water tank
27, 27' : 재수거구 28: 콤베어27, 27 ': Reclaim 28: Comveyor
29 : 연도 30: 버너29: year 30: burner
본 발명은 폐기물 특히 분리 수거가 매우 힘드는 가정용 쓰레기를 처리하는데 가장 적합하게 한 폐기물 종합 처리장치에 관한 것이다.The present invention relates to an overall waste disposal apparatus that is most suitable for treating waste, especially household waste, which is very difficult to separate.
가정용 쓰레기는 매우 습한 음식물 찌꺼기가 함유되고 있을 뿐만 아니라 난분해성인 폐섬유나 폐고무 등의 각종 고형물이 혼합되어 있어 이를 원할하게 소각한다는 것은 무척 어렵기 때문에 주로 매립처리에 의존하고 있는 실정인 바 이와 같이 매립 처리할려면 매립 용지 확보에 어려움이 있을 뿐만 아니라 트질과 지하수를 오염시키는 환경공해를 유발하게 됨으로 심각한 사희 문제로 대두되고 있는 것이다.Household waste not only contains very wet food waste, but also contains various solid materials such as waste fiber and waste rubber which are difficult to decompose, so it is very difficult to incinerate it smoothly. In order to treat landfills together, it is not only difficult to secure landfill sites but also causes environmental pollution that contaminates soil and groundwater.
본 발명은 이상의 문제점을 해결하고자 발명한 것으로 이의 발명 요지는 제1연소실에서는 음식물 찌꺼기와 폐수지 등의 가연성 쓰레기를 주로 연소시키고, 제2연소실에서는 난분해성 합성수지인 폐섬유와 폐고무 등을 완전 재연소시키고 연소과정에시 발생한 열은 폐유 재생처리 및 열병합 보일러의 열원으로 재확용하고 유해가스는 용매 처리 및 난파 유동 처리 과정을 통해 청정 공기화시키며, 용해처리 및 난파유등 처리과정에서 생긴 폐수는 오니 처리조를 통해 정화하여 열증기 발생 용수로 사용하며, 한편 순수한 음식물 찌꺼기는 퇴비가공조에서 유기질 비료를 얻고 이의 비료 처리 과정에서 생성된 메탄가스는 제2연소실의 조연 연료로서 이용할 수 있게 한 것이다.The present invention has been invented to solve the above problems, the main subject of the present invention is the first combustion chamber mainly burns combustible waste such as food waste and waste resin, and in the second combustion chamber completely regenerates waste fiber and waste rubber which are hardly decomposable synthetic resins. The heat generated during the combustion process is re-expanded as a heat source for waste oil regeneration and cogeneration boilers, and the harmful gases are converted into air through solvent treatment and wrecking flow treatment. It is purified through the treatment tank and used as heat steam generating water, while pure food waste is obtained from organic fertilizer in the compost processing tank, and the methane gas generated in the fertilizer treatment process can be used as a supporting fuel for the second combustion chamber.
이를 도면에 의거 상세히 설명하면 다음과 같다.This will be described in detail based on the drawings.
먼저 장치에 있어서 제1연소실(1)과 제2연소실(2)이 연통관(2')에 의해 서로연동되게 하고 제1, 제2연소실(1)(2)의 내주벽에는 내화 벽돌로 측조되어 있으되 이의 주벽에는 다수의 수관(5)과 송풍관(6)이 배치되어 있고 이 송풍관(6)의 일단은 송풍팬(14)과 연결되고 타단은 제1, 제2연소실(1)(2)의 내주벽에서 적당한 간격을 두고 뚫림된 노즐(4)(4')을 통해 분사되게 하였으며, 제1연소실(1)의 일측에는 호퍼(1)와 연결된 이송 스크류(1')가 부착되어 있고, 제1연소실(1)의 내저면에 설치된 불판(3)을 제1연소실(1)의 외부에 설치된 버너와 연결되며 제2연소실(2)의 상부에는 열병합 보일러(12)가 설치되어 있고, 그 하방에는 난분해 고형물 연소실(9)이 설치되어 있으되 이 연소실(9)에는 개폐문(9''')이 설치됨과 동시 공기통공(9')과 가스분사구(9)가 형성되어 있고, 제1, 제2연소실(1)(2)의 하측에는 재수거구(27)(27')가 설치되어 있으며, 난분해 고형물 연소실(9)의 좌측에는 폐유탱크(8')와 연결된 폐유 재생기(8)가 설치되어 있으되 이의 좌우측에는 폐유 분화관(8) 및 폐유기화분리실(8')이 형성되고, 그 상면에는 배출관(11')의 일단이 연결되고 이의 타단에는 정유 냉각탑(11)이 설치되어지며, 제2연소실(2)의 우측벽에는 비료가공조(23) 내에 있는 메탄가스 생성조(24)와 연결된 메탄가스 분사구(10)가 설치되어 있으며, 제1, 제2연소실(1)(2)의 저면에 설치된 재수거구(27)(27')는 콤베어(28)와 접하도록 하였으며 제2연소실(2)의 상부와 연통되게 한 사이크로톤 멀티(13)의 상부에는 덕터를 개재하여 습식냉각 장치기(16)와 연통되게 하고 습식 냉각 장치기(16) 저면의 연통부(20) ')와 연결된 난파 유동 처리기(20)의 일측에는 유해가스 정화제(19)를 장입한 장입실(19')이 설치되어 망판(19')을 개재시킨 화학 반응조(17)와 연결되어 있으되 이의 내부에는 물파쇄기(15)가 설치되어 모타(21)에 의해 고속 회전되게 하었으며, 습식 냉각장치기(16)의 공실 상부에는 분수구(16') 및 배기팬(14)의 송풍관이 연결되고 난파처리기(20)의 일측에는 연도(29)가 설치되며 습식 냉각 장치기(16)의 하부에 연결된 수관은 폐수조(26)와 연결되고 폐수조(26)에 연결된 수관은 오니 처리조(25)와 연결되어 응집실(25'), 농축실(25), 침전실(25''')을 거쳐 여과 정수조(26' )에 연결되게 한 장치이다.First, in the apparatus, the first combustion chamber 1 and the second combustion chamber 2 are connected to each other by a communication tube 2 ', and the inner circumferential walls of the first and second combustion chambers 1 and 2 are sided with fire bricks. A plurality of water pipes (5) and a blower pipe (6) are arranged on the main wall thereof, and one end of the blower pipe (6) is connected to the blower fan (14) and the other end of the first and second combustion chambers (1) (2). Injected through the nozzles 4 and 4 'bored at appropriate intervals on the inner circumferential wall, one side of the first combustion chamber 1 is attached to the transfer screw (1') connected to the hopper (1), The fire plate 3 installed on the inner bottom surface of the first combustion chamber 1 is connected to a burner installed outside the first combustion chamber 1, and the cogeneration boiler 12 is installed on the upper portion of the second combustion chamber 2. The refractory solid combustion chamber 9 is installed in the combustion chamber 9, and the combustion chamber 9 is provided with an opening and closing door 9 '' 'and an air vent 9' and a gas injection hole 9 are formed at the same time. 2 stations In the lower side of the chambers (1) and (2), re-collection holes (27) and (27 ') are provided, and on the left side of the hardly decomposed solid combustion chamber (9), a waste oil regenerator (8) connected to the waste oil tank (8') is installed. The left and right sides of the waste oil differentiation tube (8) and the waste organic matter separation chamber (8 ') is formed, one end of the discharge pipe (11') is connected to the upper side and the other end of the refinery cooling tower (11) is installed, The methane gas injection port 10 connected to the methane gas generating tank 24 in the fertilizer processing tank 23 is installed on the right side wall of the combustion chamber 2, and the first and second combustion chambers 1 and 2 The recirculation holes 27 and 27 'installed on the bottom face are in contact with the comb 28, and the wet cooling device is interposed between the upper part of the second combustion chamber 2 and the upper part of the cyclone multi 13 through the duct. A harmful gas purifier 19 is provided at one side of the wrecking flow processor 20 which is in communication with the 16 and connected to the communication part 20 ′ of the bottom of the wet cooling device 16. Charged charging chamber (19 ') is installed and connected to the chemical reaction tank (17) interposed through the net plate (19'), the water crusher (15) is installed inside the high speed by the motor (21) The upper part of the vacancy of the wet chiller 16 is connected to a blower tube 16 'and an exhaust fan 14, and a flue 29 is installed at one side of the wreckage processor 20. The water pipe connected to the lower part is connected to the waste water tank 26 and the water pipe connected to the waste water tank 26 is connected to the sludge treatment tank 25 so that the agglomeration chamber 25 ', the concentration chamber 25, and the settling chamber 25' 'are connected. Is connected to the filtration water purification tank 26 '.
이상과 같이 장치된 본 발명은 폐기물 종합처리 장치인 바 이의 처리 공정은 제1단계, 제2단계, 제3단계로 대별하여 처리되는 것으로 이의 실시예를 설명하면 다음과 같다.The present invention as described above is a waste comprehensive treatment apparatus bar treatment process is treated as a first step, a second step, a third step to explain the embodiment thereof as follows.
먼저 제1단계에 있어서 통상의 가연성 쓰레기 및 협잡물과 혼합된 음식물 찌꺼기를 호퍼(1')에 투입하면 스크류(1) 장치에 의해 제1연소실(1) 내로 강제 유입되어진다. 이때 버너(30)를 이용하여 점화시킨 후 버너(30)를 끄고 송풍팬(14')를 가동시키면 가연성 쓰레기는 송풍팬(14')에 의해 분사되는 공기속의 산소에 의해 연소되면서 고열을 발생한다.First, in the first step, when food waste mixed with ordinary combustible waste and contaminants is introduced into the hopper 1 ', it is forced into the first combustion chamber 1 by the screw 1 device. At this time, if the ignition is performed using the burner 30, the burner 30 is turned off and the blower fan 14 'is operated so that the combustible waste is burned by oxygen in the air injected by the blower fan 14' and generates high heat. .
그리고 연소과정 생성된 고열은 연통관(2')을 통해 제2연소실(2)을 가열하게 됨과 동시 제1연소실(1) 내의 수분이 함유된 음식물 찌꺼기는 건조와 동시 연소된다.The high heat generated during the combustion process heats the second combustion chamber 2 through the communication tube 2 ', and the food waste containing moisture in the first combustion chamber 1 is simultaneously burned with drying.
그리고 제2연소실(2)이 가열되면 제2연소실(2) 내에 설치된 고형물 연소실(9)은 높은 열을 갖게 된다When the second combustion chamber 2 is heated, the solid combustion chamber 9 installed in the second combustion chamber 2 has high heat.
이때 고형물 연소실(9)의 개폐문(9')을 통해 난분해성 쓰레기, 예컨데 폐섬유 폐고무 등의 고형물 등을 투입하면 이들 난분해성 쓰레기는 고형물연소실(9)의 높은 열에 의해 완전 연소된다.At this time, when the solid-decomposable waste, such as waste fiber waste rubber, is put through the opening / closing door 9 'of the solid-combustion chamber 9, these hard-decomposable waste are completely burned by the high heat of the solid-combustion chamber 9.
그리고 이때의 연소열을 이용하여 폐유를 재생시킬 수 있는 바 이는 폐유 탱크(8')로부터 이송된 폐유는 폐유 재생기(8) 내에서 가열되어 기화된 상태에서 배출관(11')을 통해 폐유 냉각탑(11)으로 이송되어 여기에서 재생되어지며, 그리고 비료가공조(13) 내에 설치된 메탄가스 생성조(24)와 연결된 메탄가스 분사구(10)에서 분사된 메탄가스의 연소에 의해 생성된 열은 제1연소실(1)에서 가열 생성된 열과 함께 합세하여 보다 높은 열을 생성시켜 전기한 개폐문(9''')으로 투입된 난연성 폐기물을 열분해시켜 완전 연소를 도우게 된다.The waste oil can be regenerated by using the heat of combustion at this time, which means that the waste oil transferred from the waste oil tank 8 'is heated in the waste oil regenerator 8 and vaporized in the waste oil cooling tower 11 through the discharge pipe 11'. The heat generated by the combustion of the methane gas injected from the methane gas injection port 10 connected to the methane gas generating tank 24 installed in the fertilizer processing tank 13 is transferred to In combination with the heat generated in (1), higher heat is generated to thermally decompose the flame retardant waste introduced into the opening / closing door (9 '' ') to help complete combustion.
그리고 전기한 연소열은 제1, 제2연소실(1)(2)의 벽면을 집중 가열시키게 되는 바 제1, 제2연소실(1)(2)의 주벽에는 내화 벽돌층이 형성되고 그 내주벽에는 여과 수조(26')와 연결된 다수의 수관(5)을 가온시킴에 따라 이때 발생된 열증기는 열병합 보일러(12)를 가열시켜 열의 재활용을 가능케 한다.In addition, the heat of the combustion heats the wall surfaces of the first and second combustion chambers 1 and 2, and a firebrick layer is formed on the circumferential wall of the first and second combustion chambers 1 and 2. As the plurality of water pipes 5 connected to the filtration tank 26 ′ is warmed, the generated heat steam heats the cogeneration boiler 12 to enable the recycling of heat.
그리고 제2단계는 공기 정화 장치인 바 이는 제2연소실(2)에서 생성된 매연등 유해가스는 사이크로톤 멀티(13)로 유입되어 집진된 후 이의 잔여 매연과 유해가스는 습식 냉각기(16)에 유입될 때 모타펌프(22)와 연결된 송수관의 분수구(16')에 의해 냉각 세정되고 이때 유해가스 속에 함유된 유동성 가스나 냄새 등 유해 물질은 화학 반응조(17)를 거치는 과정 유해가스 정화제(19)의 용액에 의해 중화 처리됨과 동시 모타에 의해 고속 회전되는 물파쇄기(15)에 의해 난파 유동 처리된 정정 공기가 되어진 상태에서 배기 연도(29)로 배출하게 된다.The second stage is an air purifier, in which harmful gases such as smoke generated in the second combustion chamber (2) are collected and collected by the cyclotone multi (13), and the residual smoke and harmful gases thereof are transferred to the wet cooler (16). When it flows in, it is cooled and washed by the water fountain 16 'of the water pipe connected to the motor pump 22. At this time, harmful substances such as fluid gas or odor contained in the harmful gas pass through the chemical reaction tank 17. Is neutralized by a solution of) and is discharged to the exhaust flue 29 in a state where the corrected air is wrecked by the water crusher 15 which is rotated at a high speed by the motor.
즉, 화학 반응조(17) 내에는 물파쇄기(15)가 고속 회전되면서 유해가스의 흡착 분해 운동을 활성화시켜 주기때문에 유해 가스는 물리적 및 화학적으로 정밀 분해되어지며, 또한 활성탄, 소석회, 녹초, 염화제2철 등의 수용액과 반응하여 중화된 후 거의 완전하게 청정된 공기가 되어진 상태에서 배기 연도(29)로 배출되기 때문에 대기를 오염시키는 일이 없어지게 된다.That is, in the chemical reaction tank 17, the water shredder 15 is rotated at a high speed to activate the adsorption decomposition movement of the harmful gas, so that the harmful gas is physically and chemically decomposed, and activated carbon, slaked lime, green grass, chloride After being neutralized by reacting with an aqueous solution such as ferric iron, the air is discharged to the exhaust flue 29 in a state where the air is almost completely clean, thereby eliminating air pollution.
그리고 제3단계는 퇴비 가공 및 정수 처리 장치인 바 이는 재2단계에서 생성된 오수 처리는 폐수조(26)와 연결된 오니 초리조(25)에서 처리하게 된다.And the third step is a compost processing and water treatment device, which is the wastewater treatment generated in the second step is treated in the sludge chorizo 25 connected to the waste water tank (26).
즉, 오니 처리조(25) 내에는 응집실(25′), 농축실(25'), 침전실(25' )에서 여과 정수되어 여과 정수조(26′)에 고이게 되며 이때 고인물은 깨끗한 상태이며, 이는 모타 펌프에 의해 펌핑되어 제1, 제2연소실(1)(2)의 벽면을 냉각시키게 된다.In other words, the sludge treatment tank 25 is filtered and purified in the coagulation chamber 25 ', the concentration chamber 25' and the settling chamber 25 'and accumulated in the filtration water purification tank 26'. , Which is pumped by a motor pump to cool the walls of the first and second combustion chambers 1, 2.
그리고 별도 수거된 음식물 찌꺼기 등은 유기질 비료로서 재처리되는 것으로 이는 퇴비 가공조(23)를 거치는 과정 발효되어 유기질 비료가 생산된다.And the food waste, which is collected separately, is reprocessed as an organic fertilizer, which is fermented through a compost processing tank 23 to produce an organic fertilizer.
이때 발생한 메탄가스는 메탄가스 생성조(24)에 모인 후 제2연소실(2)에 설치된 메탄가스 분사구(10)에 공급된다.At this time, the generated methane gas is collected in the methane gas generating tank 24 and supplied to the methane gas injection port 10 installed in the second combustion chamber (2).
그리고 제1, 제2연소실(1)(2)에서 연소된 재등의 잔여물은 재수거구(27)(27')로 토출되어진 후 콤베어(28)에 의해 수거된다.Residues, such as ash, burned in the first and second combustion chambers 1 and 2 are discharged to the re-collection ports 27 and 27 'and then collected by the conveyor 28.
이상과 같이 본 발명은 분리 수거나 분리수거가 메우 힘드는 생활쓰레기를 소각 처리함에 있어 가연성 쓰레기는 제1연소실(1)에서 소각하고, 난분해성 쓰레기는 제2연소실(2) 내에 설치된 고형물 연소실(9)에서 완전 연소되도록 하였기 때문에 혼합 쓰레기의 완전 연소처리가 가능하고, 이때 생성된 높은 열을 이용하여 폐유 재생처리를 가능하게 하였을 뿐만 아니라 연소시 발생한 유해 가스는 사이크로톤 멀티(13) 및 습식냉각기(16), 화학 반응조(17), 유해가스 정화제(19)의 수용액 및 물파쇄기(15)를 거치는 과정 유해가스 속에 함유된 유해물질이 완전 중화 및 제거되어 배기연도로 배출되고 유해가스 처리 과정에 생긴 폐수는 오니 처리조에서 정수 처리되어 재사용되게 하고 음식 찌꺼기는 유기질 비료 가공조(23)에서 발효 처리되어 양질의 유기질 비료와 메탄가스로 재활용되게 하였기 때문에 환경 공해 방지에 크게 기여할 수 있고 또한 이의 장치는 그 구조가 간단하여 소형화할 수 있어 이의 대중화에도 크게 기여할 수 있는 것이다.As described above, in the incineration process of household waste in which segregated waste or segregated waste is difficult, the combustible waste is incinerated in the first combustion chamber 1, and the hardly decomposable waste is the solid combustion chamber 9 installed in the second combustion chamber 2. ), Complete combustion treatment of mixed waste is possible, and waste oil regeneration can be performed by using the high heat generated at this time, and harmful gases generated during combustion can be recycled to cyclone multi (13) and wet coolers ( 16), the chemical reaction tank 17, the aqueous solution of the noxious gas purifier (19) and the water crusher (15) process the harmful substances contained in the harmful gas is completely neutralized and removed, discharged to the exhaust flue and generated during the harmful gas treatment process Waste water is purified by sludge treatment tank to be reused, and food waste is fermented in organic fertilizer processing tank (23) to produce high quality organic fertilizer and Since it is recycled to methane gas, it can greatly contribute to the prevention of environmental pollution, and its device can be made compact due to its simple structure and can greatly contribute to its popularization.
Claims (4)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019930028788A KR970006918B1 (en) | 1993-12-18 | 1993-12-18 | Apparatus for disposal of waste matter |
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| KR1019930028788A KR970006918B1 (en) | 1993-12-18 | 1993-12-18 | Apparatus for disposal of waste matter |
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