KR200350901Y1 - System for synthetic treatment of waste - Google Patents
System for synthetic treatment of waste Download PDFInfo
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- KR200350901Y1 KR200350901Y1 KR20-2004-0005992U KR20040005992U KR200350901Y1 KR 200350901 Y1 KR200350901 Y1 KR 200350901Y1 KR 20040005992 U KR20040005992 U KR 20040005992U KR 200350901 Y1 KR200350901 Y1 KR 200350901Y1
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- waste
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- 239000002699 waste material Substances 0.000 title claims abstract description 108
- 241000196324 Embryophyta Species 0.000 claims abstract description 138
- 239000000446 fuel Substances 0.000 claims abstract description 78
- 238000004519 manufacturing process Methods 0.000 claims abstract description 76
- 238000004064 recycling Methods 0.000 claims abstract description 48
- 239000000428 dust Substances 0.000 claims abstract description 30
- 239000010920 waste tyre Substances 0.000 claims abstract description 25
- 239000002361 compost Substances 0.000 claims abstract description 22
- 229920001971 elastomer Polymers 0.000 claims abstract description 22
- 239000005060 rubber Substances 0.000 claims abstract description 22
- 239000010893 paper waste Substances 0.000 claims abstract description 20
- 238000002485 combustion reaction Methods 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 15
- 229920003002 synthetic resin Polymers 0.000 claims abstract description 15
- 239000000057 synthetic resin Substances 0.000 claims abstract description 15
- 239000002023 wood Substances 0.000 claims abstract description 14
- 239000007789 gas Substances 0.000 claims abstract description 12
- 239000010865 sewage Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 10
- 239000010794 food waste Substances 0.000 claims abstract description 10
- 231100000719 pollutant Toxicity 0.000 claims abstract description 10
- 239000002351 wastewater Substances 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000000155 melt Substances 0.000 claims abstract description 8
- 239000000839 emulsion Substances 0.000 claims abstract description 7
- 239000012535 impurity Substances 0.000 claims abstract description 6
- 239000010985 leather Substances 0.000 claims abstract description 6
- 238000012545 processing Methods 0.000 claims abstract description 6
- 230000005611 electricity Effects 0.000 claims abstract description 5
- 239000000284 extract Substances 0.000 claims abstract description 5
- 239000002184 metal Substances 0.000 claims abstract description 5
- 229910052751 metal Inorganic materials 0.000 claims abstract description 5
- 239000011521 glass Substances 0.000 claims abstract description 4
- 235000002918 Fraxinus excelsior Nutrition 0.000 claims abstract description 3
- 240000006394 Sorghum bicolor Species 0.000 claims abstract description 3
- 235000011684 Sorghum saccharatum Nutrition 0.000 claims abstract description 3
- 239000002956 ash Substances 0.000 claims abstract description 3
- 239000010849 combustible waste Substances 0.000 claims abstract description 3
- 150000002739 metals Chemical class 0.000 claims abstract description 3
- 238000007670 refining Methods 0.000 claims abstract description 3
- 239000002341 toxic gas Substances 0.000 claims abstract description 3
- 230000032258 transport Effects 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 13
- 238000000465 moulding Methods 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims 1
- 238000010248 power generation Methods 0.000 abstract description 6
- 238000011161 development Methods 0.000 abstract description 5
- 230000002265 prevention Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 22
- 239000002994 raw material Substances 0.000 description 8
- 238000001035 drying Methods 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 6
- 230000018109 developmental process Effects 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000009264 composting Methods 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000012612 commercial material Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000009629 microbiological culture Methods 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000009740 moulding (composite fabrication) Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000010847 non-recyclable waste Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000005325 percolation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000012257 stirred material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/20—Animal feeding-stuffs from material of animal origin
- A23K10/26—Animal feeding-stuffs from material of animal origin from waste material, e.g. feathers, bones or skin
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
-
- 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
- C05F9/02—Apparatus for the manufacture
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/02—Working-up waste paper
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Polymers & Plastics (AREA)
- Molecular Biology (AREA)
- Water Supply & Treatment (AREA)
- Biotechnology (AREA)
- Health & Medical Sciences (AREA)
- Physiology (AREA)
- Animal Husbandry (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Food Science & Technology (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
본 고안은 폐기물을 종합적으로 처리하는 폐기물 광역화 종합처리시스템에 관한 것으로서, 더욱 상세하게는 각기 다른 종류의 폐기물을 처리하는 공장을 한 장소에 통합시킴으로써 부지소요를 줄이고 폐기물의 처리 경비를 대폭 절약하며, 각 단위별 공장이 필요로 하는 에너지를 자체 생산하여 상호교환함으로써 에너지를 재활용하여 부족한 에너지문제를 해소시키고, 폐기물 처리 후 매립량 절감 및 오염물질의 방출을 최소하하는 종합방지 시설을 설치하여 환경 및 산업발전에 기여할 수 있는 폐기물 광역화 종합처리시스템에 관한 것이다.The present invention relates to a waste wide area comprehensive processing system for comprehensively treating waste, and more specifically, by integrating factories for treating different kinds of waste in one place, it reduces site requirements and greatly reduces waste disposal costs. By producing and exchanging energy required by each unit's own factories, recycling energy is used to solve the insufficient energy problem, and a comprehensive prevention facility is installed to reduce landfill volume and minimize the emission of pollutants after waste disposal. The present invention relates to a comprehensive waste globalization processing system that can contribute to industrial development.
이를 위하여 본 고안은 가연성 폐기물을 이용하여 상업 및 공업용으로 활용하도록 가연성연료를 제조하는 가연성연료제조설비, 폐타이어와 고무를 용융, 기화시켜 가스를 축출하며 전력을 설비하고 발전기를 가동시켜 전기에너지를 생산하는 발전설비, 및 상기 가연성연료제조설비에서 제조된 연료를 사용하여 가동시켜 열에너지를 생산해내는 보일러 설비를 갖추어 구성된 주 공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 음식물쓰레기를 이용하여 사료를 제조하는 사료제조공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 음식물쓰레기와 축분을 이용하여 퇴비를 제조하는 퇴비제조공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐목재를 분쇄, 톱밥을 생산하여 그 톱밥을 사료와 퇴비의 부재료나 가연성연료를 만드는데 사용하고 부재료나 가연성연료제조설비에 보내는 폐목재공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐고무, 폐타이어 및 폐피혁을 분쇄하여 가연성연료제조설비에 이송시키며, 상기 폐고무, 폐타이어 및 폐피혁을 용융, 기화시켜 가스를 축출하고 전기를 발전시키는 발전설비 및 보일러를 가동시키는 보일러설비로 구성되어 전력 및 열을 공단에 공급하는 폐고무 및 폐타이어재생공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐지를 물에 용융, 금형 성형 및 재활용 재료로 생산하고, 잔유물은 가연성연료제조설비로 이송시키는 폐지재생공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐합성수지를 분쇄하고 유화액체연료를 추출하는 폐합성수지 재생공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 상기 가연성연료제조설비에서 가연성연료를 제조하고 분리된 유리 및 금속 등을 수거하여 재활용하는 재활용물질 종합수집공장 및 종합재생공장; 상기 주 공장으로부터 에너지를 공급받아 가동되고, 상기 공장들에서 재활용생산하고 발생된 2~3차 불순물을 가연성연료로 생산 및 각 공장의 열원으로 사용하고, 가연성연료로 부적합한 불순물을 1300~1800℃로 소각하여 유독가스나 악취를 완전 제거처리하는 소각연소처리공장; 상기 소각연소처리공장에서 연소시키고 남은 잔류물과 재를 매립하는 레일 덮개식 매립장; 침출수를 연계처리하는 오수 및 폐수 종합처리시설 및 정제시설과 처리된 물이 방류되는 저수시설; 분진 및 유해가스 등 오염물질을 종합처리하는 종합집진처리시설을 포함하여 구성되는 폐기물 종합처리시스템을 제공한다.To this end, the present invention is a combustible fuel manufacturing facility that manufactures combustible fuel using combustible waste for commercial and industrial use, melts and vaporizes waste tires and rubber, extracts gas, installs electric power, and operates a generator to generate electric energy. A main plant comprising a power generation facility for producing and a boiler facility for operating the fuel produced in the combustible fuel production facility to produce thermal energy; A feed manufacturing plant which is operated by receiving energy from the main plant and manufactures feed using collected food waste; A compost manufacturing plant which is operated by receiving energy from the main plant and manufactures compost by using collected food waste and sorghum; A waste wood mill which is operated by receiving energy from the main plant, crushes the collected waste wood, produces sawdust, and uses the sawdust to make feed and compost feedstock or combustible fuel, and sends the sawdust to a feedstock or combustible fuel manufacturing facility; It operates by receiving energy from the main plant, crushes the collected waste rubber, waste tire and waste leather and transports them to the flammable fuel manufacturing facility, melts and vaporizes the waste rubber, waste tire and waste leather to expel gas. A waste rubber and waste tire recycling plant composed of a power plant for generating electricity and a boiler plant for operating a boiler to supply power and heat to the industrial complex; A waste paper recycling plant which is operated by receiving energy from the main plant, produces collected waste paper in water as a melt, mold forming and recycling material, and transfers the residue to a combustible fuel manufacturing facility; A waste synthetic resin recycling plant which is operated by receiving energy from the main plant, pulverizes the collected waste synthetic resin and extracts emulsion liquid fuel; A comprehensive recycling plant and a comprehensive recycling plant, which are operated by receiving energy from the main plant, to manufacture the combustible fuel in the combustible fuel manufacturing facility, and collect and recycle separated glass and metals; It operates by receiving energy from the main plant, and produces and recycles secondary and tertiary impurities generated in the factories as combustible fuels and uses them as heat sources for each plant, and uses impurities that are not suitable as combustible fuels to 1300-1800 ° C. Incineration combustion treatment plant to completely remove toxic gas or odor by incineration; A rail-covered landfill that burns the residues and ashes burned in the incineration combustion plant; Sewage and wastewater comprehensive treatment and refining facilities linking leachate and reservoirs to which treated water is discharged; It provides a comprehensive waste treatment system that includes a comprehensive dust collection facility for comprehensive treatment of pollutants such as dust and harmful gases.
Description
본 고안은 폐기물을 종합적으로 처리하는 폐기물 종합처리시스템에 관한 것으로서, 더욱 상세하게는 각기 다른 종류의 폐기물을 처리하는 공장을 한 장소에 통합시킴으로써 부지소요를 줄이고 폐기물의 처리경비를 대폭 절감하며, 각 단위별 공장이 필요로 하는 에너지를 자체 생산하여 상호교환함으로써 에너지를 재활용하여 부족한 에너지문제를 해소시키고, 폐기물 처리 후 매립량의 대폭 절감 및 오염물질의 처리시설을 통합설비하여 시설비 절약과 오염물질 방출을 최소화하여 환경 및 산업발전에 기여할 수 있는 폐기물 종합처리시스템에 관한 것이다.The present invention relates to a waste comprehensive treatment system for comprehensively treating waste, and more particularly, by integrating factories for treating different kinds of waste in one place, reducing site requirements and drastically reducing waste disposal costs. Reuse energy by reusing energy by producing and exchanging the energy required by each plant for each unit, and drastically reduce the amount of landfill after disposal of waste and integrated facilities for the treatment of pollutants, saving facility cost and releasing pollutants The present invention relates to a total waste disposal system that can contribute to the development of the environment and industry by minimizing the amount of waste.
현대 산업사회의 급속한 발달에 따라 각종 폐기물의 발생량은 날로 증가하고 있으며, 이들을 처리하기 위하여는 재활용 또는 소멸시켜야 하는데, 관리비와 재활용처리비용, 건설비 및 부지매입비로 인하여 재활용 공장의 설립에는 자금이 많이 소요되고, 또한 현재는 재활용되는 폐기물의 종류별로 각지에 흩어진 재활용 공장에 이송하여 재활용하는 불편과 도시 미관상 비위생적이고 재활용업체의 경영악화로 부실기업이 속출하고 그 기업의 처리가 사회적 문제로 대두되고 있다.With the rapid development of the modern industrial society, the generation of various wastes is increasing day by day, and in order to dispose of them, it is necessary to recycle or extinguish them. In addition, at present, due to the inconvenience of transporting and recycling to the recycling plants scattered by various kinds of waste to be recycled, unhealthy urban management and deterioration of management of recycling companies, poor companies are emerging as social problems.
한편 폐기물을 완전히 소멸시키는 것은 기술적으로 대단히 어려워 재활용이 안되는 폐기물은 현재 소각처리하거나 해양투기 또는 매립하고 있다. 그러나 소각처리시 발생되는 오염물질은 각종의 환경오염의 원인이 되고 있어 폐기물의 80% 이상이 매립되고 있는 것이 현재 실상이다.On the other hand, it is technically very difficult to completely dispose of wastes, and non-recyclable wastes are currently incinerated, dumped or landfilled. However, pollutants generated during incineration process cause various environmental pollution, and more than 80% of wastes are currently buried.
또한 최근에는 환경문제가 세계적으로 심각하게 대두되어 공해산업의 수출금지조치와 함께 고갈되는 연료의 무기화로 산유국의 발언권이 강화되고 있으며, 산업용 연료로 사용되는 자원의 양이 한정되어 대체연료의 개발이 시급한 실정이다.In addition, in recent years, environmental problems are seriously on the rise, and the oil industry's right to speak has been strengthened due to the depletion of fuels, along with the ban on exports to the pollution industry. It is urgent.
종래 폐기물을 처리하는 동시에 연료로 사용되는 고안으로써 폐기물을 주재로 한 연료제조방법이 대한민국 특허공개 제1998-67377호에 공개되어 있다. 여기에는 동물체의 배설물과 쓰레기를 약 1:2의 비율로 혼합하여 약 15일이상 발효시킨 다음 폐지를 혼합시켜 일정량의 폐유를 투입하여 제조된 것을 특징으로 한다. 이는 폐기물을 재활용하고 제조공정상의 간단함은 있으나 폐유를 사용하여 연소시키므로 인체에 유해한 물질이 발생하여 대기오염을 가중시키므로 이를 사용하기 위해서는 폐가스의 처리장치를 설치하여야 한다.A method for manufacturing a fuel based on wastes, which is designed to be used as a fuel while treating conventional wastes, is disclosed in Korean Patent Publication No. 1998-67377. Here, the excrement and waste of the animal body is mixed at a ratio of about 1: 2, fermented for about 15 days or more, and then mixed with waste paper. This waste is recycled and is simple in the manufacturing process, but it is burned using waste oil. Therefore, it is necessary to install a waste gas treatment device in order to use it.
또한 대한민국 특허등록 제167136호에는 폐광물유와 스러찌를 이용한 연료제조방법이 등록되어있다. 여기에는 가정, 식품제조업체, 제철소, 폐차장, 제지업체, 하수처리장, 축산폐기물, 섬유업체, 방적공장 등에서 발생되는 각종폐기물을 가공처리하고 이를 고형화시켜 연료로 재활용하는 고안이 개시되어 있다.In addition, the Republic of Korea Patent Registration No. 167136 has been registered a fuel manufacturing method using waste mineral oil and sludge. It discloses a design to process and solidify various wastes generated from households, food manufacturers, steel mills, junkyards, paper companies, sewage treatment plants, livestock waste, textile companies, spinning mills, etc. and recycle them as fuel.
이 역시 폐유를 사용하여 연소시키므로 인체에 유해한 물질이 발생하여 대기오염을 가중시키므로 이를 사용하기 위해서는 폐가스의 처리장치를 설치하여야 하며, 제조과정이 복잡하여 경제성이 상실되는 문제가 있다.This also burns using waste oil, so harmful substances are generated to increase the air pollution, so in order to use them, a waste gas treatment device must be installed, and the manufacturing process is complicated and economical is lost.
또한 상기와 같은 폐기물을 이용한 연료제조방법 외에도 사료를 제조하는 방법 등 다양한 형태로 폐기물을 이용하는 방법들이 있다.In addition to the fuel manufacturing method using the waste as described above, there are methods using the waste in various forms, such as a method of manufacturing feed.
그러나, 상기 사료제조방법 역시 제조공정이 복잡하고 시설투자비, 사료의 성분, 영양성에 따라 대체사료로는 부적합하고 사료 제조 후 폐기잔재물의 발생이 많이 이를 처리하기 위해서는 소각 또는 매립하여야 하는 문제점이 발생한다.However, the feed manufacturing method also has a problem in that the manufacturing process is complicated, and it is not suitable as an alternative feed according to the facility investment cost, feed composition, nutrition, and incineration or landfill in order to deal with the generation of waste residues after the manufacture of the feed. .
한편, 상기의 폐기물 처리방법은 각 목적별로 재활용물질의 생산, 퇴비제조 또는 사료제조 등 개별적으로 실시되고 있으므로 폐기물을 종합적으로 처리하는 효율이 떨어지고, 투자성, 제조활용성, 경제성, 기술성 등이 부족하여 중도에 도산하거나 중단하는 사태가 벌어져 사회적 경제적 문제로 지적되고 있으며, 현재는 재활용 제품이 사회적 문제화되어 생산은 되나 활용이 되지 않고 있어 현재 폐기물 처리는 거의 매립에 의존하고 있다.On the other hand, the above waste treatment methods are carried out individually for the purpose of producing recycled materials, composting or feed production, so that the overall efficiency of waste treatment is inferior, and there is a lack of investment, manufacturing efficiency, economic feasibility, and technology. In the meantime, the bankruptcy or discontinuation of the situation has been pointed out as a social and economic problem. At present, recycled products become a social problem and are not produced but used. Currently, waste disposal is almost dependent on landfilling.
따라서 본 고안은 상기와 같은 문제점에 착안하여 안출한 것으로, 각기 다른 종류의 폐기물을 처리하는 공장을 한 장소에 통합시킴으로써 부지소요를 줄이고 폐기물의 처리비용을 대폭 절감하며, 각 단위별 공장이 필요로 하는 에너지를 자체생산하여 상호교환함으로써 에너지를 재활용하여 부족한 에너지문제를 해소시키고, 폐기물 처리 후 매립량을 대폭 감소시키고 오염물질의 방출을 최소하하여 환경 및 산업발전에 기여할 수 있는 폐기물 종합처리시스템을 제공함에 그 목적이 있다.Therefore, the present invention has been devised in view of the above problems, by integrating factories of different kinds of wastes in one place, reducing site requirements, drastically reducing waste disposal costs, and requiring factories for each unit. By producing and exchanging self-produced energy, recycling energy is used to solve the insufficient energy problem, and after waste disposal, waste disposal system that contributes to environment and industrial development can be greatly reduced by reducing landfill volume and minimizing the emission of pollutants. The purpose is to provide.
도 1은 본 고안의 바람직한 일실시예에 따른 폐기물 종합처리시스템의 원리를 나타낸 블록도,1 is a block diagram showing the principle of the waste comprehensive treatment system according to an embodiment of the present invention,
도 2는 본 고안의 바람직한 일실시예에 따른 주 공장과 사료제조공장과의 관계를 나타낸 블록도,Figure 2 is a block diagram showing the relationship between the main plant and the feed manufacturing plant according to an embodiment of the present invention,
도 3은 본 고안의 바람직한 일실시예에 따른 주 공장과 퇴비제조공장과의 관계를 나타낸 블록도,Figure 3 is a block diagram showing the relationship between the main plant and the compost manufacturing plant according to an embodiment of the present invention,
도 4는 본 고안의 바람직한 일실시예에 따른 주 공장과 폐목재공장과의 관계를 나타낸 블록도,Figure 4 is a block diagram showing the relationship between the main plant and waste wood mill according to an embodiment of the present invention,
도 5는 본 고안의 바람직한 일실시예에 따른 주 공장과 폐고무 및 폐타이어재생공장과의 관계를 나타낸 블록도,Figure 5 is a block diagram showing the relationship between the main plant and waste rubber and waste tire recycling plant according to an embodiment of the present invention,
도 6은 본 고안의 바람직한 일실시예에 따른 주 공장과 폐지재생공장과의 관계를 나타낸 블록도,6 is a block diagram showing the relationship between the main plant and the waste paper recycling plant according to an embodiment of the present invention,
도 7은 본 고안의 바람직한 일실시예에 따른 주 공장과 폐합성수지 재생공장과의 관계를 나타낸 블록도,Figure 7 is a block diagram showing the relationship between the main plant and waste synthetic resin recycling plant according to an embodiment of the present invention,
도 8은 본 고안의 바람직한 일실시예에 따른 주 공장과 재활용물질 종합수집공장 및 종합재생공장과의 관계를 나타낸 블록도,8 is a block diagram showing a relationship between a main plant, a recycling material comprehensive collection plant and a comprehensive recycling plant according to an embodiment of the present invention,
도 9는 본 고안의 바람직한 일실시예에 따른 주 공장과 소각연소처리공장 및 최종 매립장과의 관계를 나타낸 블록도,Figure 9 is a block diagram showing the relationship between the main plant, incineration combustion plant and final landfill in accordance with a preferred embodiment of the present invention,
도 10은 본 고안의 바람직한 일실시예에 따른 주 공장을 비롯한 공장들과 오수 및 폐수 종합처리시설 및 정제시설과 저수시설과의 관계를 나타낸 블록도,10 is a block diagram showing a relationship between factories, including a main plant, a sewage and wastewater comprehensive treatment facility, a purification facility, and a water storage facility, according to an embodiment of the present invention;
도 11은 본 고안의 바람직한 일실시예에 따른 주 공장을 비롯한 공장들과 종합집진처리시설과의 관계를 나타낸 블록도이다.11 is a block diagram showing a relationship between factories and a comprehensive dust collection facility according to an embodiment of the present invention.
*도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
100 : 주 공장 110 : 가연성연료제조설비100: main factory 110: flammable fuel manufacturing equipment
120 : 전기발전설비 130 : 보일러설비120: electric power generation equipment 130: boiler equipment
200 : 사료제조공장 300 : 퇴비제조공장200: feed manufacturing plant 300: compost manufacturing plant
400 : 폐목재공장 500 : 폐고무 및 폐타이어 재생공장400: waste wood plant 500: waste rubber and waste tire recycling plant
510 : 전기발전설비 520 : 보일러설비510: electric power plant 520: boiler
600 : 폐지재생공장 610 : 폐지분해성형설비600: Waste paper recycling plant 610: Waste paper decomposition molding equipment
700 : 폐합성수지 재생공장 710 : 유화액체연료추출설비700: Waste synthetic resin recycling plant 710: Emulsion liquid fuel extraction equipment
800 : 재활용물질 종합수집공장 810 : 종합재생공장800: comprehensive recycling plant 810: comprehensive recycling plant
900 : 소각연소처리공장 1000: 매립장900: incineration combustion plant 1000: landfill
2000: 오수 및 폐수 종합처리시설 2100: 정제시설2000: Sewage and Wastewater Treatment Plant 2100: Refinery
2200: 저수시설 3000: 종합집진처리시설2200: water storage 3000: comprehensive dust collection facility
상기와 같은 목적을 달성하기 위한 본 고안은 가연성 폐기물을 이용하여 상업 및 공업용으로 활용하도록 가연성연료를 제조하는 가연성연료제조설비, 폐타이어와 고무를 용융, 기화시켜 가스를 축출하며 전력을 설비하고 발전기를 가동시켜 전기에너지를 생산하는 발전설비, 및 상기 가연성연료제조설비에서 제조된 연료를 사용하여 가동시켜 열에너지를 생산해내는 보일러 설비를 갖추어 구성된 주 공장;The present invention for achieving the above object is a combustible fuel manufacturing equipment for producing a combustible fuel to use for commercial and industrial use by using combustible waste, melt tires and rubber by discharging, evaporate the gas, install power and generator A main plant comprising a power generation facility for producing electrical energy by operating a boiler facility and a boiler facility for producing thermal energy by operating using fuel produced by the combustible fuel manufacturing facility;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 음식물쓰레기를 이용하여 사료를 제조하는 사료제조공장;A feed manufacturing plant which is operated by receiving energy from the main plant and manufactures feed using collected food waste;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 음식물쓰레기와 축분을 이용하여 퇴비를 제조하는 퇴비제조공장;A compost manufacturing plant which is operated by receiving energy from the main plant and manufactures compost by using collected food waste and sorghum;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐목재를 분쇄, 톱밥을 생산하여 그 톱밥을 사료와 퇴비의 부재료나 가연성연료를 만드는데 사용하고 부재료나 가연성연료제조설비에 보내는 폐목재공장;A waste wood mill which is operated by receiving energy from the main plant, crushes the collected waste wood, produces sawdust, and uses the sawdust to make feed and compost feedstock or combustible fuel, and sends the sawdust to a feedstock or combustible fuel manufacturing facility;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐고무, 폐타이어 및 폐피혁을 분쇄하여 가연성연료제조설비에 이송시키며, 상기 폐고무, 폐타이어 및 폐피혁을 용융, 기화시켜 가스를 축출하고 전기를 발전시키는 발전설비 및보일러를 가동시키는 보일러설비로 구성되어 전력 및 열을 공단에 공급하는 폐고무 및 폐타이어재생공장;It operates by receiving energy from the main plant, crushes the collected waste rubber, waste tire and waste leather and transports them to the flammable fuel manufacturing facility, melts and vaporizes the waste rubber, waste tire and waste leather to expel gas. A waste rubber and waste tire recycling plant, which is composed of a power plant for generating electricity and a boiler plant for operating a boiler to supply electric power and heat to the industrial complex;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐지를 용융 및 금형 성형하여 펄프포장상자 및 재활용 재료로 생산하고, 잔유물은 가연성연료제조설비로 이송시키는 폐지재생공장;A waste paper recycling plant which operates by receiving energy from the main plant, melts and molds the collected waste paper to produce pulp packaging boxes and recycled materials, and transfers the residue to a combustible fuel manufacturing facility;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 수거된 폐합성수지를 분쇄하고 유화액체연료를 추출하는 폐합성수지 재생공장;A waste synthetic resin recycling plant which is operated by receiving energy from the main plant, pulverizes the collected waste synthetic resin and extracts emulsion liquid fuel;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 상기 가연성연료제조설비에서 가연성연료를 제조하고 분리된 유리 및 금속 등을 수거하여 재활용품을 분리수집하는 재활용물질 종합수집공장 및 종합재생공장;A comprehensive recycling plant and a comprehensive recycling plant, which are operated by receiving energy from the main plant, which manufacture a combustible fuel in the combustible fuel manufacturing facility and collect separated glass and metal to separately collect recycled materials;
상기 주 공장으로부터 에너지를 공급받아 가동되고, 상기 공장들에서 재활용생산하고 발생된 2~3차 불순물을 가연성연료로 생산 및 각 공장의 열원으로 사용하고, 가연성연료로 부적합한 불순물을 1300~1800℃로 소각하여 유독가스나 악취를 완전 제거처리하는 소각연소처리공장;It operates by receiving energy from the main plant, and produces and recycles secondary and tertiary impurities generated in the factories as combustible fuels and uses them as heat sources for each plant, and uses impurities that are not suitable as combustible fuels to 1300-1800 ° C. Incineration combustion treatment plant to completely remove toxic gas or odor by incineration;
상기 소각연소처리공장에서 연소시키고 남은 잔류물과 재를 매립하는 매립장;A landfill site for burning residues and ashes burned in the incineration combustion plant;
침출수를 연계처리하는 오수 및 폐수 종합처리시설 및 정제시설과 처리된 물이 방류되는 저수시설;Sewage and wastewater comprehensive treatment and refining facilities linking leachate and reservoirs to which treated water is discharged;
분진 및 유해가스 등 오염물질을 종합처리하는 종합집진처리시설을 포함하여 구성되는 폐기물 종합처리시스템을 제공한다.It provides a comprehensive waste treatment system that includes a comprehensive dust collection facility for comprehensive treatment of pollutants such as dust and harmful gases.
이하 본 고안을 도면에 의거하여 상세히 설명한다.Hereinafter, the present invention will be described in detail with reference to the drawings.
도 1은 본 고안의 바람직한 일실시예에 따른 폐기물 종합처리시스템의 원리를 나타낸 블록도이다.1 is a block diagram showing the principle of the waste comprehensive treatment system according to an embodiment of the present invention.
본 고안의 주 공장(100)에는 가연성연료를 제조하는 가연성연료제조설비 (110)와 상기 가연성연료제조설비(110)를 이용하여 제조된 연료를 산업에너지 및 열원으로 활용하며, 폐타이어를 용융시키고 기화가스를 축출하여 전력을 발전케하여 발전기를 가동시켜 전기에너지를 생산하는 전기발전설비(120)와, 상기 가연성연료제조설비(110)에서 제조된 연료를 열원으로 하여 보일러를 가동시켜 열에너지를 생산해내는 보일러설비(130)를 갖추고 있다.The main plant 100 of the present invention utilizes the fuel produced using the combustible fuel manufacturing facility 110 and the combustible fuel manufacturing facility 110 to manufacture the combustible fuel as an industrial energy and heat source, and melts waste tires. By discharging gaseous gas to generate electric power to operate a generator to produce electrical energy, and to produce a thermal energy by operating a boiler using the fuel produced in the combustible fuel manufacturing equipment 110 as a heat source. The inside is equipped with the boiler installation 130.
상기 주 공장(100)의 각 설비들(110, 120, 130)은 그들이 생산하는 에너지를 상호교환하면서 가동된다.Each of the facilities 110, 120, 130 of the main plant 100 operates while exchanging the energy they produce.
이 때, 상기의 가연성연료제조설비(110)에서 가연성연료가 제조되는 공정은 본 출원인이 출원한 특허출원 제2003-4414호 및 제2001-58938호에 설명된 바와 같다. 이를 살펴보면, 수거된 폐기물을 폐기물별로 분리하고 분쇄한 후 상기 분쇄물을 수분함량 10% 이하가 되도록 건조하는 단계; 상기 건조된 폐기물 중 비가연성 물질을 선별해내고 이를 다시 분쇄하는 단계; 분쇄된 재료를 보일러에 주입하여 에너지를 생산, 활용하고, 상기 분쇄물에 소석회를 투입하여 중화처리하는 단계; 상기 중화된 폐기물을 성형기에 투입하여 성형하고 최종 건조처리 및 절단하는 성형단계를 포함하여 이루어진다.At this time, the process of manufacturing the combustible fuel in the above-described combustible fuel manufacturing equipment 110 is as described in the patent application Nos. 2003-4414 and 2001-58938 filed by the present applicant. Looking at this, separating the collected waste by waste and pulverized and drying the pulverized to less than 10% moisture content; Screening non-combustible materials from the dried waste and crushing them again; Injecting the pulverized material into a boiler to produce and utilize energy, and injecting lime into the pulverized product to neutralize it; The neutralized waste is formed into a molding machine, and includes a molding step of forming and drying and cutting the final waste.
도 2는 본 고안의 바람직한 일실시예에 따른 주 공장과 사료제조공장과의 관계를 나타낸 블록도이다.Figure 2 is a block diagram showing the relationship between the main factory and the feed manufacturing plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 사료제조공장(200)이 설치되고, 사료제조가 가능한 음식물쓰레기를 투입하여 이를 분쇄 및 가공함으로써 발효사료를 제조한다.In the adjacent position of the main plant 100, the feed manufacturing plant 200 is installed, and the fermented feed is manufactured by crushing and processing the food waste into which feed can be manufactured.
상기의 발효사료를 제조하는 방법 및 장치는 본 출원인이 출원한 특허출원 제2001-58936호에 설명된 바와 같다. 이를 살펴보면, 수거된 음식물쓰레기를 분쇄하고 염분제거하는 제1단계; 상기 염분제거물을 부재료와 미생물배양균과 함께 교반하는 제2단계; 상기 교반된 물질을 45~60℃로 발효숙성 및 건조하는 제3단계; 이를 다시 65~75℃로 발효숙성 및 건조하는 제4단계; 이를 다시 80~90℃로 발효숙성 및 건조하는 제5단계; 이를 다시 95~110℃로 발효숙성 및 건조하는 제6단계를 포함하여 이루어진다.Method and apparatus for producing the fermented feed is as described in the patent application No. 2001-58936 filed by the applicant. Looking at this, the first step of crushing and desalination of the collected food waste; A second step of stirring the desalination product together with the submaterial and the microbial culture; Fermenting and drying the stirred material at 45˜60 ° C .; This fourth step of fermentation and drying to 65 ~ 75 ℃ again; A fifth step of fermenting and drying it again at 80-90 ° C .; This is made again including the sixth step of fermentation and drying at 95 ~ 110 ℃.
여기서 사료제조가 힘든 음식물쓰레기는 하기 도 3에서 설명하는 퇴비제조공장으로 이송시킨다. 퇴비제조도 불가능한 쓰레기는 주 공장(100)의 가연성연료제조설비(110)로 이송시켜 가연성연료를 제조하는 데 원료로서 사용하며, 상기 가연성연료의 원료로도 사용이 불가능한 쓰레기는 하기 도 9에서 설명되는 소각연소처리공장(900)으로 이송된다.Here, the food waste is difficult to manufacture feed to the compost manufacturing plant described in FIG. Garbage that is not compostable is also used as a raw material to produce combustible fuel by transferring it to the combustible fuel manufacturing facility 110 of the main plant 100, and the waste which cannot be used as a raw material of the combustible fuel is described in FIG. 9 below. Be transported to the incineration combustion plant (900).
상기 사료제조공장(200)의 가동에 필요한 에너지는 주 공장(100)의 가연성제조설비(110)에서 생산되는 가연성연료나 전기발전설비(120)에서 생산되는 전기에너지 또는 보일러설비(130)에서 생산되는 열에너지 중 한가지 이상을 공급받아 사용되는데, 바람직하게는 전기발전설비(120)에서 생산되는 전기에너지를 공급받아 사용하는 것이 좋다.The energy required for the operation of the feed manufacturing plant 200 is produced in the combustible fuel produced in the combustible manufacturing equipment 110 of the main plant 100 or in the electrical energy or boiler equipment 130 produced in the electrical power generation facility 120. It is used to receive one or more of the thermal energy, which is preferably used to receive the electrical energy produced by the electrical power generation facility (120).
상기 사료의 생산과정에서 증발 또는 소멸되지 않는 오수 및 폐수는 오수 및 폐수 종합처리시설(2000), 정제시설(2100) 및 저수시설(2200)로 방류된다.Sewage and wastewater that is not evaporated or extinct during the production of the feed is discharged to the sewage and wastewater comprehensive treatment facility 2000, the purification facility 2100 and the reservoir 2200.
도 3은 본 고안의 바람직한 일실시예에 따른 주 공장과 퇴비제조공장과의 관계를 나타낸 블록도이다.Figure 3 is a block diagram showing the relationship between the main plant and the compost manufacturing plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 퇴비제조공장(300)이 설치되고, 퇴비제조가 가능한 음식물쓰레기를 투입하여 이를 분쇄 및 가공함으로써 발효퇴비를 제조한다.The compost manufacturing plant 300 is installed in the adjacent position of the main plant 100, and fermented compost is manufactured by crushing and processing the compostable food waste.
상기의 발효퇴비를 제조하는 방법 및 장치는 본 출원인이 출원한 특허출원 제2001-58936호에 설명된 바와 같다. 이의 제조단계는 상기 도 2에서 설명한 바와 같다.Method and apparatus for producing the fermentation compost is as described in the patent application No. 2001-58936 filed by the applicant. Its manufacturing step is as described in FIG.
여기서 퇴비제조가 불가능한 쓰레기는 주 공장(100)의 가연성연료제조설비 (110)로 이송시켜 가연성연료를 제조하는 데 원료로서 사용하며, 상기 가연성연료의 원료로도 사용이 불가능한 쓰레기는 하기 도 9에서 설명되는 소각연소처리공장 (900)으로 이송된다.The compost can not be composted to the combustible fuel manufacturing facility 110 of the main plant 100 is used as a raw material for producing a combustible fuel, the waste that can not be used as a raw material of the combustible fuel is shown in Figure 9 below. The incineration combustion plant 900 is described.
상기 퇴비제조공장(300)의 가동에 필요한 에너지 및 퇴비제조시 발생된 오수 및 폐수의 처리는 상기 도 2에서 설명한 바와 같다.Energy required for the operation of the compost manufacturing plant 300 and the treatment of sewage and wastewater generated during the composting process are the same as described with reference to FIG.
도 4는 본 고안의 바람직한 일실시예에 따른 주 공장과 폐목재공장과의 관계를 나타낸 블록도이다.Figure 4 is a block diagram showing the relationship between the main plant and waste wood plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 폐목재공장(400)이 설치되고, 수거된 폐목재를 분쇄하여 이를 상기 사료제조공장(200) 또는 퇴비제조공장(300)으로 이송시켜 사료 또는 퇴비 제조에 사용하고, 또한 상기 분쇄된 폐목재를 상기 주 공장(100)의 가연성연료제조설비(110)로 이송하여 가연성연료를 제조하는 데 원료로써 사용한다.The waste wood plant 400 is installed at an adjacent position of the main plant 100, and the collected waste wood is crushed and transferred to the feed manufacturing plant 200 or the compost manufacturing plant 300 to feed or compost. In addition, the pulverized waste wood is transferred to the combustible fuel manufacturing facility 110 of the main plant 100 and used as a raw material for producing combustible fuel.
상기 폐목재공장(400)의 가동에 필요한 에너지는 상기 도 2에서 설명한 바와 같은 방법으로 공급받는다.Energy required for the operation of the waste wood mill 400 is supplied in the manner described in FIG.
도 5는 본 고안의 바람직한 일실시예에 따른 주 공장과 폐고무 및 폐타이어재생공장과의 관계를 나타낸 블록도이다.Figure 5 is a block diagram showing the relationship between the main plant and waste rubber and waste tire recycling plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 폐고무 및 폐타이어 재생공장(500)이 설치되고, 수거된 폐고무 및 폐타이어를 분쇄하여 이를 공업이나 상업 및 건축용 재료로 재활용하고, 다시 잔여물은 상기 주 공장(100)의 가연성연료제조설비(110)로 이송하여 가연성연료를 제조하는 데 원료로써 사용한다.Waste rubber and waste tire recycling plant 500 are installed in the adjacent position of the main plant 100, and the collected waste rubber and waste tires are pulverized and recycled to industrial, commercial and building materials, and the residue is again It is transferred to the combustible fuel manufacturing facility 110 of the main plant 100 and used as a raw material to manufacture the combustible fuel.
상기 폐고무 및 폐타이어 재생공장(500)의 가동에 필요한 에너지는 상기 도2에서 설명한 바와 같은 방법으로 공급받는다.Energy required for operation of the waste rubber and waste tire regeneration plant 500 is supplied by the method as described in FIG.
한편, 상기 폐고무 및 폐타이어 재생공장(500)에는 전기발전설비(510)와 보일러 설비(520)가 갖춰져있어, 수거된 폐고무 및 폐타이어를 열원으로 사용하여 전기발전을 하고 보일러를 가동시킨다.On the other hand, the waste rubber and waste tire regeneration plant 500 is equipped with an electric power generation equipment 510 and the boiler equipment 520, using the collected waste rubber and waste tires as a heat source to generate electricity to operate the boiler. .
도 6은 본 고안의 바람직한 일실시예에 따른 주 공장과 폐지재생공장과의 관계를 나타낸 블록도이다.6 is a block diagram showing the relationship between the main plant and the waste paper recycling plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 폐지재생공장(600)이 설치되고, 수거된 폐지를 분쇄하여 이를 상기 주 공장(100)의 가연성연료제조설비(110)로 이송하여 가연성연료를 제조하는 데 원료로써 사용한다.The waste paper recycling plant 600 is installed at an adjacent position of the main plant 100, and the collected waste paper is crushed and transferred to the combustible fuel manufacturing facility 110 of the main plant 100 to manufacture the combustible fuel. Used as a raw material.
상기 폐지재생공장(600)의 가동에 필요한 에너지는 상기 도 2에서 설명한 바와 같은 방법으로 공급받는다.Energy required for operation of the waste paper recycling plant 600 is supplied by the method as described in FIG.
한편, 상기 폐지재생공장(600)에는 폐지분해설비(610)를 갖추고 있는데, 상기 폐지분해설비(610)에서 수거된 폐지를 물에 풀어 분해하여 이를 금형설비에서 압착하고, 상기 폐고무 및 폐타이어 재생공장(500)의 보일러설비(520)를 이용하여 건조시킴으로써 화장지, 신문지, 박스용 종이 등의 재활용지류를 생산할 수 있다. 이때, 상기 분해된 폐지를 압착시의 수분은 10% 이하가 되게 건조함이 바람직하다.On the other hand, the waste paper recycling plant 600 is equipped with a waste paper decomposition equipment 610, by decomposing the waste paper collected in the waste paper decomposition equipment 610 in water to decompose it in a mold facility, the waste rubber and waste tires By using the boiler facility 520 of the regeneration plant 500, it is possible to produce recycled paper such as toilet paper, newspaper, and box paper. At this time, the water at the time of pressing the decomposed waste paper is preferably dried to 10% or less.
도 7은 본 고안의 바람직한 일실시예에 따른 주 공장과 폐합성수지 재생공장과의 관계를 나타낸 블록도이다.7 is a block diagram showing the relationship between the main plant and waste synthetic resin recycling plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 폐합성수지 재생공장(700)이 설치되고, 수거된 폐합성수지를 유화정재하여 액체연료추출설비를 비롯하여 각 공장을 가동시키는 연료로 사용하거나, 분쇄하여 공업 등 산업용 사출재료로 사용하거나, 상기 주 공장(100)의 가연성연료제조설비(110)로 이송하여 가연성연료를 제조하는 데 원료로써 사용한다.The waste synthetic resin recycling plant 700 is installed at an adjacent position of the main plant 100, and the collected waste synthetic resin is emulsified and used as fuel for operating each plant, including liquid fuel extraction facilities, or pulverized. It is used as an injection material or transferred to the combustible fuel manufacturing facility 110 of the main plant 100 and used as a raw material to manufacture the combustible fuel.
상기 폐합성수지 재생공장(700)의 가동에 필요한 에너지는 상기 도 2에서 설명한 바와 같은 방법으로 공급받는다.Energy required for operation of the waste synthetic resin recycling plant 700 is supplied in the manner described in FIG.
한편, 상기 폐합성수지 재생공장(700)에는 유화액체연료추출설비(710)를 갖추고 있는데, 상기 유화액체연료추출설비(710)에서는 합성수지에서 추출 가능한 유화액체연료를 추출하여 공업 등 산업용 연료로 사용한다.Meanwhile, the waste synthetic resin recycling plant 700 includes an emulsion liquid fuel extraction facility 710. The emulsion liquid fuel extraction facility 710 extracts an emulsion liquid fuel extractable from a synthetic resin and uses it as an industrial fuel. .
도 8은 본 고안의 바람직한 일실시예에 따른 주 공장과 재활용물질 종합수집공장 및 종합재생공장과의 관계를 나타낸 블록도이다.8 is a block diagram showing the relationship between the main plant, the recycling material comprehensive collection plant and the comprehensive recycling plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 재활용물질 종합수집공장(800)과 종합재생공장(810)이 설치되어 주 공장(100) 및 각 단위별 공장들(200,300,400,500,600, 700)에서 수거된 금속, 비철금속, 유리 등 기타 물질을 공급받는다. 이 때, 상기 재활용물질을 분리 수집하는 재활용물질 종합수집공장(800)과 이들을 자체에서 처리하는 종합재생공장(810)의 가동에 필요한 에너지는 상기 도 2에서 설명한 바와 같은 방법으로 공급받는다.In the adjacent position of the main plant 100, a comprehensive collection plant for recycling materials 800 and a comprehensive recycling plant 810 are installed, and the metals and non-ferrous metals collected from the main plant 100 and the plants for each unit (200, 300, 400, 500, 600, 700). And other materials such as glass. At this time, the energy required for the operation of the recycled material comprehensive collection plant 800 for separating and collecting the recycled material and the comprehensive regeneration plant 810 processing them are supplied in the same manner as described in FIG.
도 9는 본 고안의 바람직한 일실시예에 따른 주 공장과 소각연소처리공장과의 관계를 나타낸 블록도이다.9 is a block diagram showing the relationship between the main plant and the incineration combustion plant according to an embodiment of the present invention.
상기 주 공장(100)의 인접위치에는 소각연소처리공장(900)이 설치되어 사료제조공장(200) 및 퇴비제조공장(300)과 가연성연료제조설비(110)에서 사용할 수 없는 물질들을 공급받아 소각연소처리하게 된다. 이 때, 상기 소각연소처리공장(900)의 가동에 필요한 에너지는 상기 도 2에서 설명한 바와 같은 방법으로 공급받는다.The incineration combustion treatment plant 900 is installed in the adjacent position of the main plant 100 to incinerate materials that are not available in the feed manufacturing plant 200, the compost manufacturing plant 300, and the combustible fuel manufacturing plant 110. Combustion treatment. At this time, the energy required for the operation of the incineration combustion plant 900 is supplied in the manner described in FIG.
상기의 소각연소처리공장(900)에는 공지된 플라즈마 토치를 도입하여 폐기물을 열분해하여 다이옥신 등 유해가스를 1,300~1,500℃로 처리할 수 있다.The incineration combustion treatment plant 900 may introduce a known plasma torch to pyrolyze waste to treat harmful gases such as dioxins at 1,300 to 1,500 ° C.
소각연소처리한 후 남은 잔여물은 최종적으로 매립장(1000)으로 이송하여 레일덮개식의 위생적 매립장에 매립한다.After the incineration combustion process, the remaining residues are finally transferred to the landfill site 1000 and buried in a sanitary landfill of a rail cover type.
도 10은 본 고안의 바람직한 일실시예에 따른 주 공장을 비롯한 공장들과 오수 및 폐수 종합처리시설 및 정제시설과 저수시설과의 관계를 나타낸 블록도이다.Figure 10 is a block diagram showing the relationship between the plant, including the main plant and the sewage and wastewater comprehensive treatment facility, purification and storage facilities according to an embodiment of the present invention.
상기 주 공장(100)을 비롯한 각 단위별 공장들(200, 300, 400, 500, 600, 700, 800, 810, 900) 및 매립장(1000)에서 방출되는 오ㆍ폐수를 오수 및 폐수 처리시설(2000)에서 처리하고 정제시설(2100)에서 1급수로 정제시킨다. 이를 생명체가 있는 저수시설(2200)에 방류하여 물상태를 감정하도록 한다.Sewage and wastewater treatment facilities (e.g., wastewater and wastewater discharged from factories 200, 300, 400, 500, 600, 700, 800, 810, 900) and landfills 1000, including the main plant 100, 2000) and refined to first grade water in the refinery (2100). This is discharged to the water reservoir (2200) where the living beings are to judge the water state.
도 11은 본 고안의 바람직한 일실시예에 따른 주 공장을 비롯한 공장들과 종합집진처리시설과의 관계를 나타낸 블록도이다.11 is a block diagram showing a relationship between factories and a comprehensive dust collection facility according to an embodiment of the present invention.
상기 주 공장(100)을 비롯한 각 단위별 공장들(200, 300, 400, 500, 600, 700, 800, 810, 900)에서 발생되는 분진, 악취 및 각종 대기오염물질을 종합집진처리시설(3000)에서 처리한다.Dust collection, odor and various air pollutants generated in the plants (200, 300, 400, 500, 600, 700, 800, 810, 900) for each unit including the main plant 100, a comprehensive dust collection facility (3000) ).
상기 종합집진처리시설(3000)은 태풍의 눈을 이용한 고분자 진공집진기로써,다음의 표 1에서는 타 집진설비와 비교하였을 때의 집진율 등을 보여주고 있다.The comprehensive dust collection facility 3000 is a polymer vacuum dust collector using a typhoon eye, and Table 1 below shows dust collection rates and the like when compared with other dust collectors.
상기 표 1에서 볼 수 있듯이, 본 고안에서의 집진기의 집진율을 99.9%로써 타 집진설비와 비교하였을 때 압력손실에 비하여 분리된 입경과 집진율이 월등함을 알 수 있다.As can be seen in Table 1, when the dust collection rate of the dust collector in the present invention is 99.9%, it can be seen that the separated particle diameter and dust collection rate are superior to the pressure loss.
한편, 본 고안에서 사용된 고분자 진공집진기로 오염물질의 효율을 측정한 결과는 다음 표 2와 같다.On the other hand, the results of measuring the efficiency of contaminants with the polymer vacuum dust collector used in the present invention are shown in Table 2 below.
상기 표 2에서 볼 수 있듯이, 본 고안의 고분자 진공집진기를 가동하였을 때 오염물질의 양이 현저하게 줄었음을 볼 수 있으며 효율 역시 90%를 상회하는 수치를 보여주고 있다. 따라서 상기 집진설비를 사용한 본 고안의 폐기물 종합처리시스템에서는 오염물질이 발생되지 않아 환경보전에도 일조할 수 있다.As can be seen in Table 2, when the polymer vacuum dust collector of the present invention is operated, the amount of contaminants is markedly reduced, and the efficiency is also higher than 90%. Therefore, in the waste comprehensive treatment system of the present invention using the dust collecting facility, contaminants may not be generated, thus contributing to environmental conservation.
상기 실시예에서는 본 고안의 일실시예를 설명하였으나, 이에 국한되지 않고 본 고안의 기술적 사상을 벗어나지 않는 범위내에서 변경하여 적용할 수 있음은 당업자에게 자명한 것이다.In the above embodiment, one embodiment of the present invention has been described, but it is obvious to those skilled in the art that the present invention can be changed and applied within the scope without departing from the technical spirit of the present invention.
이상에서 설명한 바와 같이 본 고안은 각기 다른 종류의 폐기물을 처리하는공장을 한 장소에 통합시킴으로써 부지소요를 줄이고 폐기물의 처리비용을 절약하며, 각 단위별 공장이 필요로 하는 에너지를 자체 생산하여 상호교환함으로써 에너지를 재활용하여 부족한 에너지문제를 해소시키고, 폐기물 처리 후 매립량 및 오염물질의 방출을 최소하하여 환경 및 산업발전에 지대한 기여를 할 수 있는 효과가 있다.As described above, the present invention integrates factories that handle different kinds of wastes in one place to reduce site requirements, reduce waste disposal costs, and produce and exchange energy required by factories for each unit. By reusing energy, it is possible to solve the insufficient energy problem, and to minimize the amount of landfill and pollutants discharged after waste treatment, thereby making a significant contribution to environmental and industrial development.
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