KR20120078012A - Solid type fuel by wastes and a method of manufacturing the same - Google Patents
Solid type fuel by wastes and a method of manufacturing the same Download PDFInfo
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- KR20120078012A KR20120078012A KR1020100140168A KR20100140168A KR20120078012A KR 20120078012 A KR20120078012 A KR 20120078012A KR 1020100140168 A KR1020100140168 A KR 1020100140168A KR 20100140168 A KR20100140168 A KR 20100140168A KR 20120078012 A KR20120078012 A KR 20120078012A
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- 239000002699 waste material Substances 0.000 title claims abstract description 103
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000000446 fuel Substances 0.000 title description 11
- 239000007787 solid Substances 0.000 title description 6
- 239000010802 sludge Substances 0.000 claims abstract description 65
- 239000003245 coal Substances 0.000 claims abstract description 35
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 28
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 28
- 239000010794 food waste Substances 0.000 claims abstract description 28
- 239000004571 lime Substances 0.000 claims abstract description 28
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 24
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 24
- 239000010457 zeolite Substances 0.000 claims abstract description 24
- 239000010433 feldspar Substances 0.000 claims abstract description 23
- 229910052732 germanium Inorganic materials 0.000 claims abstract description 23
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 19
- 239000000654 additive Substances 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000008188 pellet Substances 0.000 claims abstract description 11
- 230000000996 additive effect Effects 0.000 claims abstract description 8
- 239000013535 sea water Substances 0.000 claims abstract description 8
- 239000002245 particle Substances 0.000 claims abstract description 5
- 239000002351 wastewater Substances 0.000 claims description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000002485 combustion reaction Methods 0.000 claims description 19
- 239000000843 powder Substances 0.000 claims description 17
- 238000001035 drying Methods 0.000 claims description 16
- 238000010298 pulverizing process Methods 0.000 claims description 15
- 238000000465 moulding Methods 0.000 claims description 10
- 238000000227 grinding Methods 0.000 claims description 9
- 239000011435 rock Substances 0.000 claims description 8
- 239000004575 stone Substances 0.000 claims description 4
- 238000004898 kneading Methods 0.000 claims 1
- 235000013305 food Nutrition 0.000 abstract 1
- 239000000123 paper Substances 0.000 description 32
- 239000003921 oil Substances 0.000 description 29
- 235000019198 oils Nutrition 0.000 description 29
- 239000010893 paper waste Substances 0.000 description 19
- 239000004449 solid propellant Substances 0.000 description 11
- 238000004064 recycling Methods 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 5
- 238000004821 distillation Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000013502 plastic waste Substances 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 2
- 231100001243 air pollutant Toxicity 0.000 description 2
- 239000002518 antifoaming agent Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000008162 cooking oil Substances 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000003063 flame retardant Substances 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000003473 refuse derived fuel Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000003440 toxic substance Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000021463 dry cake Nutrition 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- 239000004312 hexamethylene tetramine Substances 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000010705 motor oil Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920005990 polystyrene resin Polymers 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000007348 radical reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Images
Classifications
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- 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
- C10L5/403—Solid fuels essentially based on materials of non-mineral origin on paper and paper waste
-
- 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
-
- 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
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- 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
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/28—Cutting, disintegrating, shredding or grinding
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/36—Applying radiation such as microwave, IR, UV
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/40—Applying a magnetic field or inclusion of magnets in the apparatus
-
- 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
Abstract
Description
본 발명은 제지폐수슬러지를 이용한 연소물 및 그의 제조방법에 관한 것으로, 상세하게는 제지폐수슬러지와 음식물쓰레기를 함수율 50% 정도로 탈수 및 건조한 후 폐석회 및 폐석탄과 함께 100메시 이하의 입도 크기로 분쇄한 후 상기 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량% 혼합한 혼합물을 바닷물로 반죽하면서 조개탄과 같은 크기의 연소물로 성형하도록 함으로써 산업의 발달로 인해 환경을 오염시키는 제지폐수슬러지를 포함하는 폐제지슬러지를 이용하여 연소물로 제조하여 연소 중에 4500Kcal/Kg 이상의 열량을 얻을 수 있도록 한 제지폐수슬러지를 이용한 연소물 및 그의 제조방법에 관한 것이다.The present invention relates to a combusted product using paper wastewater sludge and a method for producing the same, and in particular, the paper wastewater sludge and food waste are dehydrated and dried at a water content of about 50%, and then pulverized to a particle size of 100 mesh or less with waste lime and waste coal. 20 to 60% by weight of the paper wastewater sludge crushed, 5 to 20% by weight of waste lime crushed, 5 to 25% by weight of waste coal crushed, 10 to 40% by weight of food waste crushed and 2 to 10% by weight of waste oil While mixing well the mixture of 2-10% by weight of additives of ocher crushed, elvan crushed, zeolite crushed, germanium crushed and feldspar crushed to about 100 mesh, and kneaded with seawater, It is made of combusted products using waste paper sludge including paper wastewater sludge which pollutes the environment due to the development of industry. Using a paper sludge to get the calories relates to combustion and the manufacturing method thereof.
일반적으로 산업의 발달에 따라 많은 자원이 필요로 하게 되었으며, 이를 생산하는 과정에 함량에 달하지 못하는 많은 자원이 폐기물로 분류되어 사용되지 못하여 쓰레기로 처리하여야 하는 실정이다.In general, according to the development of the industry, a lot of resources are required, and many resources that do not reach the content in the process of producing them are classified as waste and cannot be used as waste.
그러나 석탄을 캐는 과정에서 발생하는 벼력이라고도 불리는 폐석탄은 탄광촌 일대를 온통 시커먼 색으로 뒤덮을 정도로 많은 양임에도 불구하고 이를 효율적으로 처리할 수 없는 실정이다.However, although coal is called coal, which is generated in the process of digging coal, the coal coal village is large enough to cover the entire area, but it cannot be effectively processed.
또한 비료를 생산하는 과정에서 발생하는 폐석회라고도 불리는 폐비료도 비료의 생산량에 비례하여 많은 양이 계속 발생하는 데도 불구하고 이를 효율적으로 처리할 수 없는 실정이다.In addition, waste fertilizer, also called waste lime produced in the process of producing fertilizer, can not be efficiently processed even though a large amount continues to occur in proportion to the amount of fertilizer production.
마찬가지로 음식물 쓰레기와 폐유도 일부 처리하고자 하는 노력들이 많이 있지만, 이를 재활용하기 위한 방법이 극히 일부 분야에만 진행되고 있어 폐자재에 의한 피해가 점차 늘어나고 있으므로 이들 폐자재의 처리를 위한 비용도 점차 늘어가게 되는 문제점이 있었다.Similarly, there are many efforts to dispose of some food waste and waste oil, but only a few areas are being recycled, and the damage caused by waste materials is gradually increasing. There was a problem.
이에 따라 음식물쓰레기를 비롯한 난연재에 가연성 폐기물이나 가연성 물질을 혼합 성형한 RDF(refuse derived fuel), 즉 쓰레기연료가 제안되어 사용하고 있으나, 스스로 연소할 수 있는 가연제와 난연제를 혼합하여 얼마의 열량을 얻는 기술에 불과하여 폐기물 처리능력의 한계와 과도한 제작비용의 원인으로 폐기물을 근본적으로 처리하기에는 역부족이었다.Accordingly, RDF (refuse derived fuel), or waste fuel, which is formed by mixing and combusting flammable waste or combustible material with food waste is proposed and used.However, a certain amount of heat can be mixed by mixing a combustible and a flame retardant that can be burned by themselves. It was not enough technology to fundamentally dispose of waste due to the limitation of waste treatment capacity and excessive production cost.
폐제지슬러지는 제지공장의 최종과정에서 수분함량(함수율) 70 ~ 85중량%의 탈수 및 건조케익 형태로 발생되며, 수분을 제외한 고형분을 기준으로 적게는 30중량%, 많게는 70중량% 이상의 유기물이 함유되어 있다.Waste paper sludge is produced in the form of dehydration and dry cake with water content (water content) of 70 ~ 85% by weight in the final process of the paper mill.At least 30% by weight and more than 70% by weight of organic matter It is contained.
이러한 유기물의 함량으로 폐제지슬러지는 2,000kcal/kg ~ 5,000kcal/kg 정도의 열량을 가지고 있다.Waste paper sludge has a caloric content of 2,000kcal / kg ~ 5,000kcal / kg.
이에 따라, 유기성 폐제지슬러지는 저급 탄소계 연료로 분류되고 있으며, 국내의 경우 약 650만톤씩(2004년 기준) 발생하고 있다. 정부에서는 2011년 2월까지 폐제지슬러지의 해양투기를 금지하고, 재활용 등을 통한 육상처리 원칙을 발표한 바 있어, 폐제지슬러지에 대한 재활용 기술이 시도되고 있다.As a result, organic waste paper sludge is classified as a low carbon fuel, and in Korea, about 6.5 million tons are generated (as of 2004). The government banned dumping of waste paper sludge until February 2011, and announced the principle of land treatment through recycling, and recycling technology for waste paper sludge has been attempted.
폐제지슬러지의 재활용 기술은 화석연료(석탄이나 석유)의 대체연료로 활용하고자 하는 기술이 대표적이다. 그러나 폐제지슬러지는, 수분이 약 70중량% 이상을 차지하고 있어 연료화에 큰 장애가 되고 있다. 또한, 건조를 통해 수분함량을 감소시켜도 폐제지슬러지의 고형분은 연료로서의 물성을 결정하는 데 가장 중요한 휘발분의 함량과 고정탄소의 함량이 기존의 석탄계 화석연료와는 정반대의 비율로 구성되어 있어 기존의 연소 시스템에서는 연료로 활용하는 것에는 많은 제약이 따르고 있다.The recycling technology for waste paper sludge is a technology that is intended to be used as an alternative fuel for fossil fuels (coal or petroleum). However, waste paper sludge occupies about 70% by weight or more of water, which is a major obstacle to fuelization. In addition, even though the water content is reduced through drying, the solid content of the waste paper sludge is composed of the most volatile content and the fixed carbon content which are most important for determining the physical properties of the fuel as the ratio of the conventional coal-based fossil fuel. In combustion systems, there are many restrictions on the use of fuel.
한편, 폐유는 국내의 경우, 1년 약 4억L 이상이 발생하고 있다. 폐유는 폐제지슬러지에 비하여 재활용율은 높으나 주로 정제를 이용한 방법으로 재활용되고 있어 이에 따른 에너지 비용이 많이 소모된다. 폐유의 정제법은 이온정제법, 감압증류법 및 고온 열분해법 등이 있다. 이온정제법은 폐유 중 수분과 침전물을 제거하고 약품처리를 통하여 중금속 등을 제거하여 자원화하는 방법이며, 감압증류법은 박막증류 또는 탑증류 방식으로 폐유 중의 수분과 침전물 등을 제거하는 전처리 과정을 거친 후, 진공 하에서 가열 증류하는 방법이다. 그리고 고온열분해법은 폐유를 450 ~ 500℃로 가열하여 라디칼반응에 의하여 고분자를 저분자화 하여 경질유를 얻는 방법이다.On the other hand, in Korea, about 400 million liters of waste oil is generated annually. Waste oil has a higher recycling rate than waste paper sludge, but it is mainly recycled using refined methods, resulting in high energy costs. Waste oil purification methods include ion purification, vacuum distillation and high temperature pyrolysis. Ion purification method removes water and sediment from waste oil and removes heavy metals through chemical treatment, and decompression distillation method uses preliminary treatment to remove water and sediment from waste oil by thin film distillation or tower distillation. And heat distillation under vacuum. The high temperature pyrolysis method is a method of obtaining light oil by heating the waste oil at 450 to 500 ° C. to reduce the molecular weight of the polymer by radical reaction.
그러나 이들 정제법은 많은 에너지가 소모되어 과정 개선이 요구되고 있다.However, these purification methods consume a lot of energy and require improvement of the process.
상기와 같은 폐제지슬러지와 폐유의 재활용과 관련하여, 최근에는 성형성을 높이기 위하여 점토나 모래를 섞어 기존의 연탄이나 조개탄 모형으로 연료를 제조하거나, 다량의 코크스 및 석탄류를 혼합하여 고형 연료화하는 사례들이 발표되고 있다.Regarding the recycling of waste paper sludge and waste oil as described above, in recent years, in order to increase moldability, clay or sand is mixed to prepare a fuel by using conventional briquettes or briquettes, or by mixing a large amount of coke and coal to solidify the fuel. Cases are being published.
예를 들어, 한국 공개특허 제10-1991-0001084호에는 펄프 제지슬러지를 파라핀왁스에 혼합한 후 헥사민과 과망간산칼륨을 첨가하여 제조된 고형연료가 제시되어 있으며, 한국 공개특허 제10-1994-0024040호에는 나무류, 폐지류, 제지슬러지 등의 폐기물에 탄산칼슘, 제오라이트 및 결합제를 혼합한 다음, 압축 성형기를 통하여 제조된 숯 고체연료가 제시되어 있다.For example, Korean Patent Laid-Open Publication No. 10-1991-0001084 discloses a solid fuel prepared by mixing pulp paper sludge with paraffin wax and then adding hexamine and potassium permanganate, and Korean Patent Laid-Open Publication No. 10-1994- 0024040 shows a charcoal solid fuel prepared by compression molding machine after mixing calcium carbonate, zeolite and binder with waste such as wood, waste paper and paper sludge.
또한, 한국 공개특허 제10-2005-0015873호는 폐유(윤활유), 폐식용유 및 탄산가리 등을 교반하여 얻어진 결과물에 플라스틱 폐기물(폴리에틸렌, 폴리프로필렌 및 폴리스틸렌 수지)을 소량씩 분할 투입하면서 용융시켜 클로이드 수지로 만들고, 알루미늄 분쇄물 및 산화제2철 등을 혼합한 다음 냉동 건조하여 분쇄물화하는 고체연료 제조용 열량 상승물질 제조방법이 제시되어 있으며, 한국 공개특허 제10-2008-0056352호는 폐비닐이나 폐합성수지를 용융시켜 조성되는 제1연료조성물 50~60중량%와, 폐식용유와 자동차의 엔진오일 등의 폐유 그리고 흑연, 석탄 분쇄물, 폐목재나 톱밥을 혼합 압출시켜 조성되는 제2연료조성물 20~30중량%, 그리고 결합제인 규산소다 10~15중량%로 혼합하여 구성한 고체연료가 제시되어 있다.In addition, Korean Patent Application Publication No. 10-2005-0015873 discloses a plastic waste (polyethylene, polypropylene, and polystyrene resin) that is melted in small portions in a resultant product obtained by stirring waste oil (lubricating oil), waste cooking oil, and carbonate. A method of producing a calorie-raising material for producing a solid fuel, which is made of an Lloyd resin, mixed with an aluminum pulverized product and ferric oxide, and then freeze-dried to form a pulverized product, is disclosed in Korean Patent Application Publication No. 10-2008-0056352. 50 to 60% by weight of the first fuel composition formed by melting waste synthetic resin, waste oil such as waste oil such as used cooking oil and engine oil of automobile, and second fuel composition formed by mixing and extruding graphite, coal pulverized product, waste wood or sawdust 20 A solid fuel composed of 30 wt% and 10-15 wt% binder sodium silicate is shown.
아울러, 일본 공개특허 소56-62891호에는 유기성 슬러지, 폐유 및 플라스틱 폐기물을 혼합, 성형한 다음, 열 건조를 통하여 수분함량을 낮춘 고체연료의 제조방법이 제시되어 있으며, 일본 공개특허 평2001-214173호에는 가열된 식물성 기름에 폐기 종이기저귀 등의 폐기물을 투입하여 수분을 증발시키고, 상기 폐기물에 함유된 염화수소 가스를 염화칼슘에 중화 제거한 후, 폐유를 첨가하여 제조한 액상 또는 과립상의 연료가 제시되어 있다.In addition, Japanese Patent Laid-Open No. 56-62891 discloses a method for producing a solid fuel in which organic sludge, waste oil, and plastic waste are mixed and molded, and then lowered in water content by thermal drying, and Japanese Patent Laid-Open No. 2001-214173 No. 6 shows liquid or granular fuel prepared by adding waste oil such as waste paper diapers to heated vegetable oil, evaporating water, neutralizing and removing hydrogen chloride gas contained in the waste, and adding waste oil. .
그러나 상기 선행특허문헌들은 포함한 종래의 기술은 서로 상이한 물성의 재료가 섞여있어 연소의 최적 조건을 맞추기가 힘들뿐 아니라 발열량이 낮고, 불완전연소 등으로 인한 각종 유독물질(및 대기오염물질)이 배출되며, 불연성 재료가 첨가되어 있어 연소가 어렵다. 또한, 석탄 분쇄물이나 석유 코크스 분쇄물을 열량보강재로 첨가하는 방법은 제지슬러지의 열량을 높이기 위하여 열량보강재를 제지슬러지 고형분에 대하여 적게는 1.25배, 많게는 45배 가까이 첨가하고 있어, 이는 열량보강재에 제지슬러지를 첨가하는 형태가 되어 폐제지슬러지의 활용도가 떨어지는 문제점이 있다. 아울러, 한국 공개특허 제10-2005-0015873호 및 일본 공개특허 소56-62891호 등에서와 같이 바인더로서 플라스틱 폐기물을 사용하는 경우, 연소 시 다이옥신, 염소, 황 등의 유독물질(및 대기오염물질)의 배출량이 많아 고체연료로서 갖춰야 할 조건(자원절약과 재활용 촉진에 관한 법률 제25조의3 제2항 관련)을 만족하지 못하는 문제점이 있다.However, the prior art including the prior patent documents are mixed with materials of different physical properties, it is difficult to meet the optimum conditions of combustion, low calorific value, various toxic substances (and air pollutants) due to incomplete combustion, etc. Non-combustible materials are added and combustion is difficult. In addition, the method of adding coal pulverized or petroleum coke pulverized as calorific reinforcement is to add calorie reinforcement to the paper sludge solids at least 1.25 times and as much as 45 times to increase the calorie content of the paper sludge, which is added to the calorie reinforcement. There is a problem in that the utilization of the waste paper sludge is reduced to form the paper sludge. In addition, in the case of using plastic waste as a binder as in Korean Patent Application Publication No. 10-2005-0015873 and Japanese Patent Application No. 56-62891, etc., toxic substances (and air pollutants) such as dioxin, chlorine and sulfur during combustion are used. There is a problem in that it does not satisfy the conditions to be provided as solid fuel (related to Article 25-3 (2) of the Act on Resource Conservation and Recycling Promotion) due to the large amount of emissions.
한편, 폐유와 수분(폐제지슬러지에 함유된 수분)이 혼합된 상태에서 성형 및 건조되는 경우, 증발된 수분이 폐유의 기름막을 통과하면서 엄청난 양의 기포를 발생시킨다. 구체적으로, 압출(압축) 성형 및 건조 과정에서는 열이 공급되는데, 이때 열에 의해 수분이 증발되어 기포가 발생된다. 그러나 상기 선행특허문헌들을 포함한 종래 기술은 상기 기포 방지를 위한 기술적 수단을 강구하지 못하여, 압출(압축) 성형 과정에서 기포 발생에 의해 압출(압축)이 어렵고, 제품(고체연료)의 성형성(형태 유지성)이 떨어지고, 건조 후 공극이 형성되는 문제점이 있다. 또한, 종래의 고체연료는 원료 함량의 최적화 및 상기 기포 방지(공극 형성 방지)를 고려하지 못하여 제품의 물성(강도 등)이 저하되어 취급이 어려운 문제점이 지적된다. 즉, 강도 저하로 인하여 고체연료의 저장 및 운송 시 깨짐에 의한 분진 발생으로 취급이 어렵다.On the other hand, when molded and dried in a state where waste oil and water (water contained in waste paper sludge) are mixed, evaporated water passes through the oil film of waste oil to generate a huge amount of bubbles. Specifically, heat is supplied during extrusion (compression) molding and drying, where moisture is evaporated by heat to generate bubbles. However, the prior art including the prior patent documents do not take the technical means for preventing the bubble, it is difficult to extrude (compress) by the generation of bubbles in the extrusion (compression) molding process, the formability of the product (solid fuel) Maintainability) is lowered, there is a problem that voids are formed after drying. In addition, the conventional solid fuel does not consider the optimization of the raw material content and the bubble prevention (preventing the formation of voids) is pointed out a problem that the physical properties (strength, etc.) of the product is lowered, difficult to handle. That is, it is difficult to handle due to the generation of dust due to cracks during storage and transportation of the solid fuel due to the strength decrease.
그리하여 2009년 01월 22일자 특허출원 제10-2009-0005524호(폐제지슬러지와 폐유를 이용한 고체연료 및 그 제조방법)가 제안되었으며,Therefore, Patent Application No. 10-2009-0005524 dated January 22, 2009 (solid fuel using waste paper sludge and waste oil and its manufacturing method) was proposed.
이는, 폐제지슬러지, 폐유, 바인더 및 기포방지제를 포함하되, 폐제지슬러지 고형분 100중량부를 기준으로 폐유 5 ~ 40중량부, 바인더 3~ 20중량부 및 기포방지제 0.1 ~ 5중량부를 포함하는 혼합물을 제조하는 제1단계;This includes waste paper sludge, waste oil, a binder and an anti-foaming agent, and includes a mixture containing 5 to 40 parts by weight of waste oil, 3 to 20 parts by weight of the binder and 0.1 to 5 parts by weight of the antifoaming agent, based on 100 parts by weight of the waste paper sludge solids. A first step of manufacturing;
상기 제1단계에서 제조된 혼합물을 반고체상태의 성형체로 성형하는 제2단계;A second step of molding the mixture prepared in the first step into a semi-solid molded body;
상기 제2단계에서 성형된 반고체상태의 성형체를 수분함량 0.01 ~ 10중량%가 되도록 건조하는 제3단계를 포함하여 구성하였다.It was configured to include a third step of drying the semi-solid molded body formed in the second step to a moisture content of 0.01 to 10% by weight.
상기와 같은 폐제지슬러지와 폐유를 이용한 고체연료 및 그 제조방법에 의하여서는 폐지슬러지나 폐유와 같은 유기성 폐기물의 가연성 재료만 이용하도록 하였으므로 난연성 폐기물을 별도로 처리할 수 없게 되는 단점이 있었다.The solid fuel using the waste paper sludge and the waste oil as described above and the method of manufacturing the same are used only to combustible materials of organic waste such as waste paper sludge or waste oil, so that the flame retardant waste cannot be separately processed.
이에 본 발명은 상기한 바와 같은 종래의 문제점을 해소하기 위한 것으로, 제지폐수슬러지와 음식물쓰레기를 함수율 50% 정도로 탈수 및 건조한 후 폐석회 및 폐석탄과 함께 100메시 이하의 입도 크기로 분쇄한 후 상기 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량% 혼합한 혼합물을 바닷물로 반죽하면서 펠릿 형태의 연소물로 성형하도록 함으로써 산업의 발달로 인해 환경을 오염시키는 제지폐수슬러지를 이용하여 연소물로 제조하여 연소 중에 4500Kcal/Kg 이상의 열량을 얻을 수 있도록 한 제지폐수슬러지를 이용한 연소물 및 그의 제조방법을 제공하는 것을 그 목적으로 한다.Accordingly, the present invention is to solve the conventional problems as described above, after dewatering and drying the paper wastewater sludge and food waste to about 50% water content and then crushed to a particle size of 100 mesh or less with waste lime and waste coal after the 20 to 60% by weight of paper wastewater sludge crushing, 5 to 20% by weight of waste lime crushing, 5 to 25% by weight of waste coal crushing, 10 to 40% by weight of food waste crushing, and 2 to 10% by weight of waste oil The mixture of 2-10% by weight of additives of ocher crushed, elvan crushed, zeolite crushed, germanium crushed and feldspar crushed, each of which was pulverized to about 100 mesh, was kneaded with seawater and formed into a pellet-like combustion product. Paper wastewater sludge manufactured by burning products using paper wastewater sludge that pollutes the environment due to the development of the industry, and obtains more than 4500Kcal / Kg of heat during combustion The combustion products and to provide a method of manufacturing the same for that purpose.
상기 목적을 달성하기 위한 본 발명의 제지폐수슬러지를 이용한 연소물 및 그의 제조방법은,Combustion product using the papermaking wastewater sludge of the present invention and its manufacturing method for achieving the above object,
제지폐수슬러지를 탈수기와 건조기에서 함수율 50% 미만으로 탈수 및 건조하는 과정과,Dewatering and drying the paper wastewater sludge in a dehydrator and dryer at a water content of less than 50%;
음식물쓰레기를 탈수기와 건조기에서 함수율 50% 미만으로 탈수 및 건조하는 과정과,Dehydrating and drying the food waste to less than 50% water content in the dehydrator and dryer,
폐석회를 건조기에서 건조하는 과정과,Drying the waste lime in a dryer,
상기의 제지폐수슬러지를 분쇄기에서 100메시 정도로 분쇄하여 제지폐수슬러지 분쇄물을 제조하는 과정과,Preparing a paper wastewater sludge pulverized product by grinding the paper wastewater sludge to about 100 mesh in a mill;
상기의 음식물쓰레기를 분쇄기에서 100메시 정도로 분쇄하여 음식물쓰레기 분쇄물을 제조하는 과정과,Preparing a food waste pulverized product by pulverizing the food waste at about 100 mesh in a crusher;
상기의 건조한 폐석회를 100메시 정도로 분쇄하여 폐석회분쇄물을 제조하는 과정과,Pulverizing the dry waste lime to about 100 mesh to prepare a waste lime crushed,
폐석탄을 100메시 정도로 분쇄하여 폐석탄 분쇄물을 제조하는 과정과,Pulverizing the waste coal to about 100 mesh to produce a waste coal pulverized,
황토를 100메시 정도로 분쇄하여 황토 분쇄물을 제조하는 과정과,Crushing the loess to about 100 mesh to produce the loess crushed,
맥반석을 100메시 정도로 분쇄하여 맥반석 분쇄물을 제조하는 과정과,Pulverizing the elvan rock to about 100 mesh to manufacture the elvan rock crushed,
제올라이트를 100메시 정도로 분쇄하여 제올라이트 분쇄물을 제조하는 과정과,Grinding the zeolite to about 100 mesh to prepare a zeolite pulverized product,
게르마늄을 100메시 정도로 분쇄하여 게르마늄석 분쇄물을 제조하는 과정과Crushing germanium to about 100 mesh to produce germanium crushed powder and
장석을 100메시 정도로 분쇄하여 장석 분쇄물을 제조하는 과정과,Pulverizing feldspar to about 100 mesh to produce feldspar pulverized material,
상기의 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물을 동일한 분량으로 혼합하여 첨가제를 제조하는 과정과,A process of preparing an additive by mixing the above-mentioned ocher crushed, elvan pulverized, zeolite pulverized, germanium pulverized and feldspar pulverized in the same amount;
상기의 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량% 혼합하여 혼합물을 제조하는 과정과,20 to 60% by weight of the paper wastewater sludge pulverized product, 5 to 20% by weight waste lime crushed product, 5 to 25% by weight waste coal pulverized product, 10 to 40% by weight food waste pulverized product and 2 to 10% by weight waste oil Preparing a mixture by mixing 2 to 10% by weight of additives of ocher crushed, ganban stone crushed, zeolite crushed, germanium crushed and feldspar crushed, each of which is pulverized to about 100 mesh with good mixing;
상기의 혼합물을 바닷물로 반죽하면서 펠릿 성형기로 펠릿 형태의 연소물로 성형하도록 함으로써 산업의 발달로 인해 환경을 오염시키는 제지폐수슬러지 등의 폐기물을 이용하여 연소물로 제조하여 연소 중에 4500Kcal/Kg 이상의 열량을 얻을 수 있도록 구성함을 특징으로 한다.The above mixture is kneaded with sea water to form pellets in the form of pellets in a pellet forming machine to produce combustion products using waste such as paper wastewater sludge that pollutes the environment due to the development of the industry to obtain more than 4500 Kcal / Kg of heat during combustion. It is characterized by the configuration so that it can be.
상기와 같은 본 발명의 제지폐수슬러지를 이용한 연소물 및 그의 제조방법에 의하여서는 각각 탈수 및 건조시킨 제지폐수슬러지와 음식물쓰레기, 건조시킨 폐석회 및 폐석탄 각각 100메시 정도로 분쇄하고,The combusted product using the papermaking wastewater sludge of the present invention as described above and the manufacturing method thereof are ground to about 100 mesh, respectively, dehydrated and dried paper wastewater sludge and food waste, dried waste lime and waste coal, respectively,
황토, 맥반석, 제올라이트, 게르마늄석 및 장석을 100메시 정도로 분쇄하고,Crush the loess, elvan, zeolite, germanium and feldspar to about 100 mesh,
상기의 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량%를 잘 혼합하여 혼합물을 제조하고,20 to 60% by weight of the paper wastewater sludge pulverized product, 5 to 20% by weight waste lime crushed product, 5 to 25% by weight waste coal pulverized product, 10 to 40% by weight food waste pulverized product and 2 to 10% by weight waste oil The mixture was prepared by mixing 2-10 wt% of the additives of the loess pulverized, ganbanite crushed, zeolite crushed, germanium crushed and feldspar crushed, each of which was ground to about 100 mesh with good mixing.
상기의 혼합물 90?95중량%에 바닷물 5?10중량%를 부으면서 반죽하여 펠릿 형태의 연소물로 성형하도록 함으로써 이를 일반 석탄이나 무연탄과 같이 연소물로 사용할 수 있는 효과가 있다.The mixture is kneaded while pouring 5-10 wt% of seawater into 90 to 95 wt% of the mixture to form a pellet in the form of a combustion product, which can be used as a combustion product such as general coal or anthracite coal.
도 1은 본 발명의 제조 과정을 도시한 개략도. 1 is a schematic diagram illustrating a manufacturing process of the present invention.
이하, 첨부된 도면을 참조하여 본 발명의 바람직한 실시예를 설명하면 다음과 같다.Hereinafter, preferred embodiments of the present invention will be described with reference to the accompanying drawings.
본 발명에 따른 제지폐수슬러지를 이용한 연소물의 제조방법은,The production method of the combustion product using the papermaking wastewater sludge according to the present invention,
제지폐수슬러지를 탈수기와 건조기에서 함수율 50% 미만으로 탈수 및 건조하는 과정과,Dewatering and drying the paper wastewater sludge in a dehydrator and dryer at a water content of less than 50%;
음식물쓰레기를 탈수기와 건조기에서 함수율 50% 미만으로 탈수 및 건조하는 과정과,Dehydrating and drying the food waste to less than 50% water content in the dehydrator and dryer,
폐석회를 건조기에서 건조하는 과정과,Drying the waste lime in a dryer,
상기의 제지폐수슬러지를 분쇄기에서 100메시 정도로 분쇄하여 제지폐수슬러지 분쇄물을 제조하는 과정과,Preparing a paper wastewater sludge pulverized product by grinding the paper wastewater sludge to about 100 mesh in a mill;
상기의 음식물쓰레기를 분쇄기에서 100메시 정도로 분쇄하여 음식물쓰레기 분쇄물을 제조하는 과정과,Preparing a food waste pulverized product by pulverizing the food waste at about 100 mesh in a crusher;
상기의 건조한 폐석회를 분쇄기에서 100메시 정도로 분쇄하여 폐석회분쇄물을 제조하는 과정과,Preparing the waste lime grind by pulverizing the dry waste lime to about 100 mesh in a grinder,
폐석탄을 분쇄기에서 100메시 정도로 분쇄하여 폐석탄 분쇄물을 제조하는 과정과,Pulverizing the waste coal in the crusher to about 100 mesh to produce the waste coal pulverized,
황토를 100메시 정도로 분쇄하여 황토 분쇄물을 제조하는 과정과,Crushing the loess to about 100 mesh to produce the loess crushed,
맥반석을 100메시 정도로 분쇄하여 맥반석 분쇄물을 제조하는 과정과,Pulverizing the elvan rock to about 100 mesh to manufacture the elvan rock crushed,
제올라이트를 100메시 정도로 분쇄하여 제올라이트 분쇄물을 제조하는 과정과,Grinding the zeolite to about 100 mesh to prepare a zeolite pulverized product,
게르마늄을 100메시 정도로 분쇄하여 게르마늄석 분쇄물을 제조하는 과정과Crushing germanium to about 100 mesh to produce germanium crushed powder and
장석을 100메시 정도로 분쇄하여 장석 분쇄물을 제조하는 과정과,Pulverizing feldspar to about 100 mesh to produce feldspar pulverized material,
상기의 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물을 동일한 분량으로 혼합하여 첨가제를 제조하는 과정과,A process of preparing an additive by mixing the above-mentioned ocher crushed, elvan pulverized, zeolite pulverized, germanium pulverized and feldspar pulverized in the same amount;
상기의 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량%를 부으면서 반죽하여 펠릿 성형기를 통해 펠릿 형태의 성형물로 성형하는 과정과,20 to 60% by weight of the paper wastewater sludge pulverized product, 5 to 20% by weight waste lime crushed product, 5 to 25% by weight waste coal pulverized product, 10 to 40% by weight food waste pulverized product and 2 to 10% by weight waste oil While mixing well, the additives of ocher crushed, elvan crushed, zeolite crushed, germanium crushed, and feldspar crushed, each of which is crushed to about 100 mesh, are kneaded with 2-10% by weight, and formed into pellet-shaped moldings through a pellet forming machine. Process,
상기의 성형물을 건조하여 연소물로 제조하는 과정들로 구성한 것이다.It is composed of the process of drying the molding to produce a combustion product.
상기와 같은 본 발명에 따른 제지폐수슬러지를 이용한 연소물의 제조방법은,The production method of the combustion product using paper wastewater sludge according to the present invention as described above,
제지폐수슬러지를 제1 탈수기에서 함수율 60?70%로 탈수한 후 다시 제1 건조기에서 함수율 50% 미만으로 건조한다.The paper wastewater sludge is dewatered at a moisture content of 60 to 70% in the first dehydrator and then dried again to less than 50% in a first dryer.
음식물쓰레기를 제2 탈수기에서 함수율 60?70%로 탈수한 후 다시 제2 건조기에서 함수율 50% 미만으로 건한다.The food waste is dehydrated at a moisture content of 60 to 70% in the second dehydrator and then dried again to less than 50% in the second dryer.
폐석회를 제3 건조기에서 건조한다.Waste lime is dried in a third dryer.
상기의 제지폐수슬러지를 제1 분쇄기에서 100메시 정도로 분쇄하여 제지폐수슬러지 분쇄물을 제조한다.The paper wastewater sludge is pulverized in a first mill to about 100 mesh to prepare paper wastewater sludge crushed products.
상기의 음식물쓰레기를 제2 분쇄기에서 100메시 정도로 분쇄하여 음식물쓰레기 분쇄물을 제조한다.The food waste is ground to about 100 mesh in a second mill to prepare a food waste pulverized product.
상기의 건조한 폐석회를 제3 분쇄기에서 100메시 정도로 분쇄하여 폐석회분쇄물을 제조한다.The dry waste lime is pulverized in a third mill to about 100 mesh to prepare waste lime grind.
폐석탄을 제4 분쇄기에서 100메시 정도로 분쇄하여 폐석탄 분쇄물을 제조한다.Waste coal is pulverized in a fourth mill to about 100 mesh to produce waste coal pulverized product.
황토를 제4 분쇄기에서 100메시 정도로 분쇄하여 황토 분쇄물을 제조한다.The ocher is pulverized in a fourth mill to about 100 mesh to produce an ocher pulverized product.
맥반석을 제4 분쇄기에서 100메시 정도로 분쇄하여 맥반석 분쇄물을 제조한다.Elvan rock is pulverized in a fourth mill to about 100 mesh to produce a lamellar grinding.
제올라이트를 제4 분쇄기에서 100메시 정도로 분쇄하여 제올라이트 분쇄물을 제조한다.Zeolite is ground in a fourth mill to about 100 mesh to prepare a zeolite pulverized product.
게르마늄을 제4 분쇄기에서 100메시 정도로 분쇄하여 게르마늄석 분쇄물을 제조하는 과정과The process of manufacturing germanium stone pulverized by grinding germanium to about 100 mesh in the fourth mill and
장석을 제4 분쇄기에서 100메시 정도로 분쇄하여 장석 분쇄물을 제조한다.Feldspar is prepared by grinding feldspar to about 100 mesh in a fourth mill.
상기의 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물을 동일한 분량으로 제1 혼합기에서 혼합하여 첨가제를 제조한다.The ocher pulverized product, elvan pulverized product, zeolite pulverized product, germanium pulverized product and feldspar pulverized product are mixed in the same amount in a first mixer to prepare an additive.
상기의 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량%를 제2 혼합기에서 혼합하여 혼합물을 제조한다.20 to 60% by weight of the paper wastewater sludge pulverized product, 5 to 20% by weight waste lime crushed product, 5 to 25% by weight waste coal pulverized product, 10 to 40% by weight food waste pulverized product and 2 to 10% by weight waste oil The mixture is prepared by mixing 2 to 10% by weight of the additives of the loess crushed, gantholite crushed, zeolite pulverized, germanium pulverized and feldspar pulverized with about 100 mesh with good mixing in a second mixer.
상기의 혼합물 90?95중량%에 바닷물 5?10중량%를 반죽기에 부으면서 반죽하여 펠릿 성형기를 통해 펠릿 형태의 성형물로 성형한다.90 to 95% by weight of the mixture is kneaded while pouring 5 to 10% by weight of seawater into a kneader to form a molding in pellet form through a pellet molding machine.
상기의 성형물을 제4 건조기에서 건조하여 연소물로 제조함으로써 산업의 발달로 인해 환경을 오염시키는 제지폐수슬러지를 이용하여 연소물로 제조하여 연소 중에 4500Kcal/Kg 이상의 열량을 얻을 수 있도록 한다.The molded product is dried in a fourth dryer and manufactured as a combusted product, so that the calcined product may be manufactured using combustible wastewater sludge that pollutes the environment due to industrial development, so that calories of 4500 Kcal / Kg or more may be obtained during combustion.
Claims (2)
음식물쓰레기를 탈수기와 건조기에서 함수율 50% 미만으로 탈수 및 건조하는 과정과,
폐석회를 건조기에서 건조하는 과정과,
상기의 제지폐수슬러지를 분쇄기에서 100메시 정도로 분쇄하여 제지폐수슬러지 분쇄물을 제조하는 과정과,
상기의 음식물쓰레기를 분쇄기에서 100메시 정도로 분쇄하여 음식물쓰레기 분쇄물을 제조하는 과정과,
상기의 건조한 폐석회를 분쇄기에서 100메시 정도로 분쇄하여 폐석회분쇄물을 제조하는 과정과,
폐석탄을 분쇄기에서 100메시 정도로 분쇄하여 폐석탄 분쇄물을 제조하는 과정과,
황토를 100메시 정도로 분쇄하여 황토 분쇄물을 제조하는 과정과,
맥반석을 100메시 정도로 분쇄하여 맥반석 분쇄물을 제조하는 과정과,
제올라이트를 100메시 정도로 분쇄하여 제올라이트 분쇄물을 제조하는 과정과,
게르마늄을 100메시 정도로 분쇄하여 게르마늄석 분쇄물을 제조하는 과정과
장석을 100메시 정도로 분쇄하여 장석 분쇄물을 제조하는 과정과,
상기의 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물을 동일한 분량으로 혼합하여 첨가제를 제조하는 과정과,
상기의 제지폐수슬러지 분쇄물 20?60중량%, 폐석회 분쇄물 5?20중량%와 폐석탄 분쇄물 5?25중량%와 음식물쓰레기 분쇄물 10?40중량% 및 폐유 2?10중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?10중량%를 혼합하여 혼합물을 제조하는 과정과,
상기의 혼합물 90?95중량%에 바닷물 5?10중량%를 부으면서 반죽하여 펠릿 성형기를 통해 펠릿 형태의 성형물로 성형하는 과정과,
상기의 성형물을 건조하여 연소물로 제조하는 과정으로 구성한 것을 특징으로 하는 제지폐수슬러지를 이용한 연소물의 제조방법.Dewatering and drying the paper wastewater sludge in a dehydrator and dryer at a water content of less than 50%;
Dehydrating and drying the food waste to less than 50% water content in the dehydrator and dryer,
Drying the waste lime in a dryer,
Preparing a paper wastewater sludge pulverized product by grinding the paper wastewater sludge to about 100 mesh in a mill;
Preparing a food waste pulverized product by pulverizing the food waste at about 100 mesh in a crusher;
Preparing the waste lime grind by pulverizing the dry waste lime to about 100 mesh in a grinder,
Pulverizing the waste coal in the crusher to about 100 mesh to produce the waste coal pulverized,
Crushing the loess to about 100 mesh to produce the loess crushed,
Pulverizing the elvan rock to about 100 mesh to manufacture the elvan rock crushed,
Grinding the zeolite to about 100 mesh to prepare a zeolite pulverized product,
Crushing germanium to about 100 mesh to produce germanium crushed powder and
Pulverizing feldspar to about 100 mesh to produce feldspar pulverized material,
A process of preparing an additive by mixing the above-mentioned ocher crushed, elvan pulverized, zeolite pulverized, germanium pulverized and feldspar pulverized in the same amount;
20 to 60% by weight of the paper wastewater sludge pulverized product, 5 to 20% by weight waste lime crushed product, 5 to 25% by weight waste coal pulverized product, 10 to 40% by weight food waste pulverized product and 2 to 10% by weight waste oil Preparing a mixture by mixing 2 to 10% by weight of additives of ocher pulverized powder, elvan pulverized powder, zeolite pulverized powder, germanium pulverized powder and feldspar pulverized, each of which is pulverized to about 100 mesh with good mixing;
The process of kneading while pouring 5 to 10% by weight of seawater to 90 to 95% by weight of the mixture to form a molding in the form of pellets through a pellet molding machine,
A method for producing a combusted product using paper-making wastewater sludge, characterized in that the molding is dried to produce a combusted product.
100메시 이하로 각각 분쇄한 황토분말, 맥반석분말, 제올라이트분말, 게르마늄석분말 및 장석분말을 각각 동일한 분량으로 혼합하여 첨가제를 제조하고,
상기 제지폐수슬러지 분쇄물 30?50중량%, 폐석회 분쇄물 10?15중량%와 폐석탄 분쇄물 10?20중량%와 음식물쓰레기 분쇄물 20?30중량% 및 폐유 3?7중량%를 잘 혼합하면서 100메시 정도로 각각 분쇄한 황토 분쇄물, 맥반석 분쇄물, 제올라이트 분쇄물, 게르마늄석 분쇄물 및 장석 분쇄물의 첨가제를 2?5중량% 혼합하여 혼합물을 제조하고,
상기의 혼합물 90?95중량%에 바닷물 5?10중량%를 부으면서 반죽하여 펠릿 형태로 성형물로 성형한 후 건조하여 구성한 것을 특징으로 하는 제지폐수슬러지를 이용한 연소물.Dehydrated and dried paper wastewater sludge with about 50% water content, food waste, dry waste lime and waste coal, and crushed to a particle size of less than 100 mesh,
An additive is prepared by mixing the same quantity of ocher powder, ganban stone powder, zeolite powder, germanium stone powder and feldspar powder, respectively, which are ground to 100 mesh or less.
30 to 50% by weight of the paper wastewater sludge crushed, 10 to 15% by weight of waste lime crushed, 10 to 20% by weight of waste coal crushed, 20 to 30% by weight of food waste crushed and 3 to 7% by weight of waste oil A mixture was prepared by mixing 2 to 5% by weight of additives of ocher crushed powder, ganban rock crushed powder, zeolite pulverized powder, germanium crushed powder and feldspar crushed powder, respectively.
Combustion product using papermaking wastewater sludge, characterized in that the mixture was kneaded while pouring 5-10% by weight of sea water in 90 to 95% by weight of the mixture, and then formed into a molded product in the form of pellets and dried.
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KR20160112349A (en) * | 2015-03-19 | 2016-09-28 | 윤종길 | Manufacturing method of fuel pellet comprising wasted organics |
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KR20160112349A (en) * | 2015-03-19 | 2016-09-28 | 윤종길 | Manufacturing method of fuel pellet comprising wasted organics |
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