KR20020066315A - The Apparatus of Recycling Wastes for a Substitute Energy and the Manufacturing Process - Google Patents
The Apparatus of Recycling Wastes for a Substitute Energy and the Manufacturing Process Download PDFInfo
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- KR20020066315A KR20020066315A KR1020020043718A KR20020043718A KR20020066315A KR 20020066315 A KR20020066315 A KR 20020066315A KR 1020020043718 A KR1020020043718 A KR 1020020043718A KR 20020043718 A KR20020043718 A KR 20020043718A KR 20020066315 A KR20020066315 A KR 20020066315A
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- 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
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/04—Garbage
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- 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
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
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- 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
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Abstract
Description
본 발명은 산업체 일반폐기물 중 고열가(8000Kcal/Kg이상)의 폐기물(합성수지, 합성고무, P.E 등)을 폐목제 칩(Chip)과 2:1의 비율로 혼합, 건조하여 중열량가(5000Kcal/Kg정도)의 대체에너지로 이용할 수 있도록 성형부에서 일정규격의 고형물을 제조하는 방법과 그 장치에 관한 것이다.The present invention mixes and drys high-temperature waste (synthetic resin, synthetic rubber, PE, etc.) with waste wood chips (Chip) in a ratio of 2: 1 among general wastes of industrial wastes (about 5000Kcal / Kg). The present invention relates to a method and apparatus for manufacturing a solid of a certain standard in a molding part so that it can be used as an alternative energy.
종래의 산업체 일반폐기물의 처리는 일부 선별하여 재활용제품의 원료로 사용하고 상태가 불량하거나 이물질의 혼합정도가 큰 것은 소각, 매립 등의 방법으로 처리하였으나 불완전연소로 인해 대기오염 및 악취발생의 요인이 될 뿐 아니라 지역주민들의 NIMBY현상 확산으로 소각장 및 매립장 건립이 어려우므로 이에 대한 대책의 일환으로 상기의 폐기물을 이용하여 대체에너지용 고형연료로 자원화 하고자 하는 것이다.Conventional industrial wastes are partially selected and used as raw materials for recycled products. Poor conditions or large mixing of foreign substances are treated by incineration, landfilling, etc. In addition, it is difficult to build incinerators and landfills due to the proliferation of NIMBY phenomena among local residents, and as a countermeasure, the wastes will be used as solid energy for alternative energy.
한편 일부 관심있는 업자들이 여러 방법으로 폐기물을 성형하여 대체에너지화 하려는 노력을 기울였으나 분리수거미흡, 선별미흡, 원료의 균질·균일한 배합미숙 등으로 인하여 조잡한 성형에 이르는 것은 물론 대체에너지용으로 연소할 때 내용물이 녹아 흘러내리거나 숯덩이(char)상태가 되어 완전연소가 불가능하였다. 이러한 불완전연소는 다이옥신 발생의 원인이 되었고 이것이 사회적 환경문제를 또다시 유발시키는 부정적 효과를 가져왔다.In the meantime, some interested companies have tried to make alternative energy by shaping waste in various ways, but it is not only poor coarse molding due to lack of segregation collection, poor selection, raw material homogeneous and uniform mixing, but also combustion for alternative energy. When the contents melted or flowed down or became char, it was impossible to burn completely. This incomplete combustion caused dioxins, which had a negative effect on the social environment.
상기와 같은 문제점을 해결하고 실용화할 수 있는 방안으로써 본 발명은 사업장별 폐기물의 분리수거와 폐기물의 특성에 따른 일정비율의 성분별 혼합수거 및 폐목재 칩(Chip)혼합의 정량화로 성형제품 연소시 흘러내림 방지는 물론숯덩이(char) 상태의 탄화막 피복형성을 방지하여 고형연료를 완전연소시킴으로써 유해 폐가스의 배출을 방지하며, 또한 목재칩 건조공정(9)의 건조 열원으로 본 공정에서 제조된 고형폐기물을 열분해 연소하여 발생하는 연소열을 이용하고 이때 건조공정(9)에서 배출되는 폐열을 혼합원료 건조공정(13)에 재이용하는 재활용 자원화에 목적이 있다.In order to solve the above problems and put them into practical use, the present invention is to separate the wastes of each business site and to separate the wastes at a certain ratio according to the characteristics of the wastes and to quantify the waste wood chip mixing. It prevents runoff and prevents the formation of char film coverings in the char state to completely burn out the solid fuel to prevent the emission of harmful waste gases and also as a drying heat source in the wood chip drying process (9). The purpose of the present invention is to use recycling heat generated by pyrolytic combustion of waste, and to recycle the waste heat discharged from the drying process (9) in the mixed raw material drying process (13).
상기의 목적을 이루기 위한 과제로서 사업장의 고분자화합물인 폐기물과 폐목재 칩을 중량혼합비 2:1의 비율로 혼합하는 혼합조정공정(10)을 거쳐 균일한 원료로 혼합하는 한편 폐기물의 열분해 연소시에 발생하는 NOx, SOx, 염소(Cl) 등의 환경유해물질 발생을 억제 또는 방지하기 위하여 첨가제(중화제인 석회)를 분사투입장치(12a)에 의해 혼합원료에 투입한 후 혼합원료 공급공정(12)과 폐열이용 건조공정(13)을 거쳐 고형화 성형공정(14)에서 재활용 대체연료로 사용할 수 있도록 Ø30m/mxL50m/m사이즈의 성형제품을 제조하는 방법이다.In order to achieve the above object, through the mixing and adjusting step (10) of mixing waste wood chips and waste wood chips in the workplace at a weight mixing ratio of 2: 1, the raw materials are mixed into uniform raw materials, In order to suppress or prevent the generation of environmentally harmful substances such as NOx, SOx, and chlorine (Cl), an additive (lime as a neutralizer) is introduced into the mixed raw material by the injection dosing device 12a, and then the mixed raw material supply process 12 It is a method of manufacturing a molded product of Ø30m / mxL50m / m size to be used as a recycled alternative fuel in the solidification molding process 14 through the waste heat and drying process (13).
특히 건조공정(13)에서는 목재칩 건조장치(9)에서 발생하는 폐열을 열공급원으로 이용하여 수분함량 15%로 건조하게 되는데 이때에 버너의 직열을 투입하거나 간접열이라도 킬른(Kiln) 내부의 온도가 150℃이상이 되면 합성 고분자화합물인 원료가 가소성이 되어 벽에 전착되는 경우가 있으므로 이를 방지하고 건조효율을 높임은 물론 자원의 재활용 차원에서 건조공정(9)의 폐열(220℃∼250℃)을 이용하는 시스템에 의하여 연료절감의 효과를 가져오는 폐기물의 재활용 자원화 플랜트이다.In particular, in the drying process (13), the waste heat generated from the wood chip drying apparatus (9) is used as a heat source to dry with 15% moisture content. At this time, the temperature inside the kiln is input even if the burner is directly heated or indirectly heated. When the temperature is above 150 ℃, the raw material, which is a synthetic polymer compound, may be plasticized and deposited on the wall. Therefore, the waste heat of the drying process 9 (220 ℃ ~ 250 ℃) can be prevented and the drying efficiency can be improved. It is a waste recycling plant that produces fuel savings by using a system.
도1은 본 발명에 따른 재활용 시스템과 고형연료 제조공정도면1 is a drawing showing a recycling system and a solid fuel manufacturing process according to the present invention.
도2는 열분해 연소열 이용장치 및 폐열이용 건조시스템Figure 2 is a pyrolysis combustion heat using device and waste heat drying system
도3은 원료의 유압식 정량공급과 스크류식 압출성형공정도면Figure 3 is a hydraulic quantitative supply of screw and screw extrusion molding process drawing
***도면중 주요 부분에 대한 부호의 설명****** Description of the symbols for the main parts of the drawings ***
1 : 산업폐기물 적치장 2 : 이송선별공정1: Industrial waste stockpile 2: Transfer sorting process
3 : 1차파쇄공정 4 : 자석선별공정3: primary crushing process 4: magnet sorting process
5 : 2차파쇄공정 6 : 폐목재 적치장5: secondary crushing process 6: waste stockyard
7 : 절단선별공정 8 : 목재칩 파쇄공정7: cutting screening process 8: wood chip shredding process
9 : 2중구조건조공정 90 : 고형연료 열분해 연소장치9: dual-ball conditioning process 90: solid fuel pyrolysis combustion device
10 : 혼합저장공정 11 : 3차파쇄공정10: mixed storage process 11: tertiary shredding process
12 : 혼합원료공급공정 13 : 폐열이용건조공정12: Mixed raw material supply process 13: Waste heat utilization drying process
14 : 성형공정 12a : 중화제 분사투입장치14: forming process 12a: neutralizer injection injection device
이하 첨부된 도면에 의하여 본 발명을 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
도1의 공정에 따른 본 발명은 산업체에서 발생하는 일반폐기물과 건설현장에서 발생하는 폐목재를 재활용하여 대체에너지용 고형연료로 제조하는 방법을 나타낸 것으로, 분리수거된 폐기물(합성수지, 합성고무, 함성섬유, P.E 등)을 저장·적치하는 적치부(1)와 폐기물에 혼재하여있는 금속류, 불연물을 인력으로 선별하는 이송선별공정(2)과 선별된 원료를 100m/m 사이즈로 절단·파쇄하는 1차파쇄공정(3)과 상기 파쇄된 원료중 선별되지 않은 금속류를 제거하기 위한 자석선별공정(4)과 50m/m 사이즈로 파쇄하는 2차파쇄공정(5)을 거쳐 폐기물의 1단계 원료화 전처리 공정이 끝나고 혼합저장부(10)에 이송된다.The present invention according to the process of Figure 1 shows a method for producing a solid fuel for alternative energy by recycling the general waste generated from the industry and the waste wood generated in the construction site, the waste collected separately (synthetic resin, synthetic rubber, cryogenic Storage part (1) for storing and loading fibers, PE, etc.) and a transfer screening process (2) for sorting metals and non-combustibles mixed in the wastes by manpower and 1 for cutting and crushing the selected raw materials to a size of 100 m / m. First stage raw material pretreatment of waste through a third crushing process (3), a magnet screening process (4) for removing unselected metals from the crushed raw materials, and a second crushing process (5) for crushing at a size of 50 m / m The process ends and is transferred to the mixed storage unit 10.
한편 부원료인 폐목재 칩(Chip) 제조공정에 대하여 설명하면 건설현장에서 수거된 폐목재를 적치장(6)에 종류와 크기에 따라 분류·적치하고 절단성형공정(7)에서 파쇄작업이 용이하도록 절단 및 가지치기 등의 전처리 작업을 행한 후 목재파쇄, 칩제조공정(8)에서 30m/m∼50m/m 사이즈로 파쇄하고 2중구조 드럼형 건조장치(9)에서 수분함량 20%이하로 건조·조정한 후 상기 2종류의 원료를 혼합하기 위한 혼합용 공정(10)으로 이송하여 2차파쇄공정(5)을 거친 폐기물과 함수량 20%이하인 폐목재 칩을 중량비 2:1의 비율로 혼합하는 중간원료 혼합공정에 이른다.On the other hand, the waste wood chip manufacturing process, which is an auxiliary material, will be described and sorted according to the type and size of the waste wood collected at the construction site according to the type and size of the stockyard (6) and cut to facilitate the crushing operation in the cutting molding process (7). After pretreatment such as pruning and pruning, the wood is shredded to 30 m / m to 50 m / m in the shredding and chip manufacturing process (8) and dried to less than 20% moisture content in the double drum type drying machine (9). After the adjustment, the mixture is transferred to the mixing step 10 for mixing the two kinds of raw materials, and the waste which has undergone the secondary crushing step 5 and the waste wood chips having a water content of 20% or less are mixed at a weight ratio of 2: 1. It leads to raw material mixing process.
상기의 혼합공정(10)을 거친 혼합원료는 3차파쇄공정(11)에서 평균 30m/m의 사이즈로 파쇄한 후 가공원료 공급호퍼(Hopper)(12)에 이송되는데 이때에 성형폐기물의 연소시 발생하는 유해배기가스인 다이옥신의 배출을 억제 또는 감소시키기 위하여 중화제(석회) 분사투입장치(12a)에서 석회를 혼합원료대비 2%정도 분사투입혼합함으로써 혼합원료 건조시와 고형연료 성형 및 연소시에 발생하는 NOx, SOx, Cl화물을 중화시키는 역할을 한다.The mixed raw material that has passed through the mixing process 10 is crushed to an average size of 30 m / m in the tertiary crushing process 11 and then transferred to the processing raw material supply hopper 12, where the burning of the molding waste is performed. In order to suppress or reduce the emission of dioxin, which is a harmful exhaust gas, lime is injected and mixed about 2% of the mixed raw material in the neutralizer (lime) injection dosing device 12a to dry the mixed raw materials and to form and burn solid fuel. It neutralizes the generated NOx, SOx and Cl.
상기의 공정을 거친 중간저장 공급호퍼(Hopper)(12)의 혼합원료를 드럼(Drum)형 건조장치(13)에서 수분함량 15%정도로 건조하여 유압식 정량공급장치에 의해 공급하면 스크류식 압출성형공정(14)에서 성형하고 이를 절단하여 Ø30m/mxL50m/m 사이즈의 고형화 연료를 생산하는 폐기물의 재활용 방법이다.When the mixed raw material of the intermediate storage feed hopper 12 passed through the above process is dried in a drum type drying apparatus 13 to about 15% of water and supplied by a hydraulic metering feeder, it is a screw type extrusion molding process. It is a recycling method of waste which is molded in (14) and cut to produce solidified fuel of Ø30m / mxL50m / m size.
상기의 재활용 방법을 공정별로 설명하면 폐기물의 적치장(1)은 수거된 폐기물을 종류별로 2∼3파트로 분류·적치하여 원료공급을 가능한 균질화하는 공정이고, 폐목재의 적치장(6)은 수거된 폐목재를 크기별로 구분·적치하여 절단공정(7)을 거쳐야하는 것과 그렇지 않은 것을 구분함으로써 칩 제조공정(8)의 작업효율을 높이는 폐원료의 분류공정이다.When the above recycling method is explained by process, the waste stockyard 1 is a process of classifying and placing the collected waste into 2 to 3 parts for each type to homogenize the supply of raw materials, and the stockyard 6 of the waste wood is collected. It is a classification process of waste raw materials that improves the work efficiency of the chip manufacturing process (8) by classifying and placing the waste wood by the size and sorting the waste wood (7).
폐기물의 이송컨베이어 선별공정(2)은 폐기물에 혼재되어있는 금속류, 돌, 흙 등의 불연물을 선별하여 파쇄기의 칼날을 보호하고, 성형화 과정에서의 효율과 제품의 질을 높이기 위하여 사람이 수작업으로 선별·제거·처리하는 공정이다.Waste conveying conveyor sorting process (2) sorts incombustibles such as metals, stones, and soil mixed in the wastes to protect the blade of the crusher, and to improve the efficiency and product quality in the molding process, It is a process of sorting, removing and processing.
1차파쇄공정(3)은 인력으로 선별·처리된 폐기물을 100m/m의 사이즈로 파쇄하는 공정으로써 혼재하고 있는 폐기물의 형질을 조정하는 전처리 단계의 공정이다.The primary crushing step (3) is a step of crushing waste sorted and treated by manpower to a size of 100 m / m, which is a step of pretreatment step of adjusting the characteristics of mixed wastes.
자력선별공정(4)은 상기 선별과정에서 분리·선별되지 않은 금속류를 자력에 의하여 선별하는 공정으로써 철금속, 비철금속 등을 선별·회수하며, 2차파쇄공정(5)에서 폐기물 원료를 50m/m의 사이즈로 파쇄하고 폐목재 칩과 2:1의비율로 혼합하기 위해 혼합 저장공정(10)의 사일로(Silo)에 이송하여 혼합원료를 만드는 공정이다.The magnetic screening process (4) is a process for selecting metals that are not separated or selected in the screening process by magnetic force. The magnetic screening process selects and recovers ferrous metals and non-ferrous metals, and the waste raw material is 50m / m in the secondary crushing process (5). In order to mix the waste wood chips with a ratio of 2: 1, the raw materials are transferred to silos of the mixed storage process 10 to make mixed raw materials.
폐목재의 절단공정(7)은 적치장(6)에서 크거나 긴 사이즈로 분류된 폐목재를 절단, 가지치기 등의 작업으로 목재칩제조 파쇄장치(8)에서의 작업성을 용이하게 하고 생산효율을 높이기 위한 전처리 공정이며, 폐목재 칩의 크기를 30m/m∼50m/m로 파쇄하는 공정이다.The cutting process of waste wood (7) facilitates workability in the wood chip manufacturing shredding device (8) by cutting and pruning the waste wood classified into large or long size in the stockyard (6). It is a pretreatment step for increasing the size of the chips, and is a step of crushing the size of the waste wood chip to 30m / m to 50m / m.
도2에서 보는바와 같이 2중구조 드럼형 건조공정(9)은 화석연료를 사용하지않고 고형 폐기물 연료를 열원으로 하는 재활용 건조장치로써, 열분해 연소장치(90)에서 고형연료를 저산소상태(요구산소량의 60∼70% 공급)인 1차연소실에서 450℃~650℃의 온도를 유지하며 열분해시키고 이때 열분해된 미연소가스를 2차연소실(91)에서 이론 요구 공기량보다 과잉으로 공급하여 미연소가스를 완전연소시킴과 동시에 배기온도를 850℃이상 유지하여 배기하고 이 배기열을 2중구조 드럼형 건조공정(9)의 열원으로 이용하는 화석연료 대체용의 폐기물 재활용 시스템에 의한 건조공정이며 이때 수분함량 20%이하로 건조한다.As shown in FIG. 2, the dual-structure drum-type drying process 9 is a recycling drying apparatus using solid waste fuel as a heat source without using fossil fuel, and in the pyrolysis combustion apparatus 90, the solid fuel is in a low oxygen state (required oxygen amount). Pyrolysis while maintaining the temperature of 450 ℃ ~ 650 ℃ in the primary combustion chamber (60 ~ 70% of the supply), and the unburned gas is supplied by supplying the pyrolyzed unburned gas in excess of the theoretical required air amount in the secondary combustion chamber (91) It is a drying process by waste recycling system for replacing fossil fuel that uses complete combustion and maintains the exhaust temperature above 850 ℃ and uses this exhaust heat as heat source of the double-structure drum type drying process (9). It is dried below.
원료혼합 저장공정(10)은 2차파쇄공정(5)을 거친 폐기물 원료와 2중구조 건조공정(9)을 거친 폐목재 칩을 혼합 조정하는 시스템으로써 이때 폐기물과 목재칩의 혼합비율은 중량비 2:1로 하여 2종류의 원료를 균일·균질하게 하는 공정이다.The raw material mixing storage process (10) is a system for mixing and adjusting waste raw materials which have undergone the secondary crushing process (5) and waste wood chips which have undergone the dual structure drying process (9), wherein the mixing ratio of waste and wood chips is weight ratio 2 It is a process of making two types of raw materials uniform and homogeneous as 1: 1.
상기 공정에서 혼합된 원료는 3차파쇄공정(11)으로 이송하여 30m/m의 크기로 파쇄하고 다시 혼합원료 공급공정(12)에 이송하며 이때에 중화제 분사투입장치(12a)를 통하여 석회를 원료에 분사투입하고 혼합함으로써 혼합원료의건조 및 성형공정(14)에서 발생할 수 있는 NOx, Sox, 염소(Cl)화물 등을 중화하여 다이옥신 발생을 억제 내지 방지시켜 환경유해가스 배출을 저지하는 특징을 갖는 공정이다.The raw material mixed in the above process is transferred to the tertiary crushing process 11, and crushed to a size of 30 m / m, and then transferred to the mixed raw material supply process 12. At this time, the lime is fed through the neutralizer injection dosing device 12a. Injection and mixing to neutralize NOx, Sox, chlorine (Cl), etc., which may occur in the drying and molding process of mixed raw materials, thereby inhibiting or preventing the generation of dioxin, thereby preventing environmentally harmful gas emissions. It is a process.
3차파쇄공정(11)과 중화제 분사투입 후 혼합공정(12)을 거친 원료는 수분함량을 15% 정도로 조정하기 위하여 건조공정(13)을 거치게 되는데 이때 건조장치에 공급되는 열원은 폐목재칩(Chip) 건조공정(9)에서 발생·배기되는 220℃∼250℃의 배기폐열을 이용하고 이때에 건조킬른(Kiln) 내부온도가 150℃내외에서 건조되도록 조절되어야 한다. 이것은 고분자화합물인 산업체 일반폐기물의 건조온도가 150℃이상이 되면 원료의 열분해 현상이 일어남과 동시에 일부 가소성이 되어 킬른 내부 벽면에 부착됨으로써 건조기능의 상실은 물론 적정한 고형연료 제조의 원료로써 부적절한 덩어리 상태가 되기 때문에 킬른 내부의 온도가 항상 일정하게 유지되도록 자동온도 조절장치를 부착한 건조공정이다.After the third crushing process (11) and the neutralizing agent injection, the raw material that passed through the mixing process (12) is subjected to a drying process (13) to adjust the water content to about 15%, wherein the heat source supplied to the drying apparatus is waste wood chips ( Chip) The waste heat of 220 ° C to 250 ° C generated and exhausted in the drying process 9 should be used, and the temperature inside the drying kiln should be controlled to be dried at around 150 ° C. When the drying temperature of industrial waste, which is a high molecular compound, is higher than 150 ℃, thermal decomposition of raw materials occurs and at the same time, it is partially plasticized and attached to the inner wall of the kiln. This is a drying process with a thermostat so that the temperature inside the kiln is always kept constant.
특히 혼합원료 건조공정(13)은 2중구조 드럼형 건조공정(9)에서 배기되는 220℃∼250℃의 배기폐열을 대체에너지로 이용하여 건조하는 공정으로써, 간접열에 의해 로 내부의 온도를 150℃정도로 조정 건조하여 혼합원료 중 고분자화합물이 열분해하는 것을 방지하고, 열가소성에 의하여 로 벽에 전착되는 것을 막기 위한 자동온도 제어장치가 부착된 로터리 드럼형 건조장치와 일정량 원료공급장치로 구성된 건조공정이다.In particular, the mixed raw material drying step 13 is a step of drying the waste heat of 220 ° C. to 250 ° C. exhausted in the double drum type drying step 9 as an alternative energy. It is a drying process consisting of a rotary drum type drying device equipped with an automatic temperature control device and a certain amount of raw material supply device to prevent thermal decomposition of the polymer compound in the mixed raw material by adjusting and drying to about ℃ and preventing electrodeposition to the furnace wall by thermoplastic. .
성형공정(14)은 혼합원료 건조공정(13)에서 건조된 함수율 15%정도인 혼합원료를 고형화하는 공정으로써, 도3에서 보는바와 같이 고형화 성형시스템(14)은 유압식 정량공급장치(14a), 스크류식 압출성형장치(14b), 그리고 일정사이즈로 절단하는 절단장치(14c) 등으로 구성되어 있으며, 특히 성형과정에서 발생하는 원료의 열분해 배기가스는 2중구조 건조장치(9)에 재투입하여 재연소의 공정을 거침으로써 배기 폐가스의 배출을 최대한 억제하는 장치로 구성된 공해방지효과 및 폐기물의 재활용 자원화의 고형연료 제조방법이다.The molding step 14 is a step of solidifying the mixed material having a moisture content of about 15% dried in the mixed material drying step 13, and as shown in FIG. 3, the solidifying molding system 14 includes a hydraulic metering device 14a, It consists of a screw extrusion molding device 14b and a cutting device 14c for cutting to a certain size. In particular, the pyrolysis exhaust gas of the raw material generated during the molding process is re-injected into the double structure drying device 9. It is a method of manufacturing solid fuel with pollution prevention effect composed of a device that minimizes emission of exhaust waste gas by going through the reburn process and recycling of waste resources.
이상에서 설명한 바와 같이 산업체에서 배출되는 고분자화합물과 건설현장에서 배출되는 폐목재를 상호 재이용하여 대체에너지로 자원화 할 수 있는 시스템과 방법에 관한 것으로써, 생산된 고형연료를 열분해 연소장치(90)에 의한 폐가스 연소열을 상기 건조공정의 열원으로 재이용하는 특징과 특히 건조공정(9)에서 배출되는 배기폐열을 혼합원료 건조공정(13)에서 재이용하고 또한 배기가스를 재연소에 의하여 완전연소시켜 배출하는 대기오염방지에도 역점을 두어 폐기물을 대체에너지로 재활용하는 방법으로써의 그 효과가 있다.As described above, the present invention relates to a system and a method for recycling a high-molecular compound discharged from an industry and waste wood discharged from a construction site into alternative energy. The produced solid fuel is transferred to a pyrolysis combustion apparatus 90. The waste gas combustion heat is reused as a heat source of the drying process, and in particular, the waste waste heat discharged from the drying process (9) is reused in the mixed raw material drying process (13), and the exhaust gas is completely burned and discharged by re-burning. There is also an effect as a method of recycling waste as alternative energy, with an emphasis on pollution prevention.
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KR102237280B1 (en) * | 2020-09-14 | 2021-04-07 | 아세아시멘트(주) | Waste pre-treatment in-line system for continuous in-put of combustible wastes as substitution fuel in cement calcination facilities |
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