KR20140087334A - A solid fuel using a mix waste and a preparation method thereof - Google Patents
A solid fuel using a mix waste and a preparation method thereof Download PDFInfo
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- KR20140087334A KR20140087334A KR20120157225A KR20120157225A KR20140087334A KR 20140087334 A KR20140087334 A KR 20140087334A KR 20120157225 A KR20120157225 A KR 20120157225A KR 20120157225 A KR20120157225 A KR 20120157225A KR 20140087334 A KR20140087334 A KR 20140087334A
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- 239000002699 waste material Substances 0.000 title claims abstract description 84
- 239000004449 solid propellant Substances 0.000 title claims abstract description 59
- 238000002360 preparation method Methods 0.000 title description 4
- 239000002023 wood Substances 0.000 claims abstract description 85
- 239000000203 mixture Substances 0.000 claims abstract description 82
- 239000000446 fuel Substances 0.000 claims abstract description 76
- 239000010802 sludge Substances 0.000 claims abstract description 51
- 239000010812 mixed waste Substances 0.000 claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 claims abstract description 37
- 239000010865 sewage Substances 0.000 claims abstract description 30
- 229920002554 vinyl polymer Polymers 0.000 claims description 57
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 56
- 238000000465 moulding Methods 0.000 claims description 32
- 210000003608 fece Anatomy 0.000 claims description 29
- 239000010871 livestock manure Substances 0.000 claims description 29
- 229920001131 Pulp (paper) Polymers 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 17
- 238000002156 mixing Methods 0.000 claims description 12
- 239000006148 magnetic separator Substances 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 230000005484 gravity Effects 0.000 claims description 7
- 239000010786 composite waste Substances 0.000 claims description 4
- 229920005830 Polyurethane Foam Polymers 0.000 claims 1
- 239000011496 polyurethane foam Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 claims 1
- -1 sawdust Substances 0.000 abstract description 10
- 239000000843 powder Substances 0.000 abstract description 9
- 229920003023 plastic Polymers 0.000 abstract description 3
- 239000004033 plastic Substances 0.000 abstract description 3
- 239000002689 soil Substances 0.000 abstract 1
- 238000002474 experimental method Methods 0.000 description 13
- 235000013312 flour Nutrition 0.000 description 11
- 238000012360 testing method Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 8
- 238000010298 pulverizing process Methods 0.000 description 8
- 239000002131 composite material Substances 0.000 description 7
- 230000000704 physical effect Effects 0.000 description 7
- 229920003002 synthetic resin Polymers 0.000 description 6
- 239000000057 synthetic resin Substances 0.000 description 6
- 239000002916 wood waste Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 239000005022 packaging material Substances 0.000 description 4
- 238000007711 solidification Methods 0.000 description 4
- 230000008023 solidification Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- HMUNWXXNJPVALC-UHFFFAOYSA-N 1-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C(CN1CC2=C(CC1)NN=N2)=O HMUNWXXNJPVALC-UHFFFAOYSA-N 0.000 description 1
- 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
- LDXJRKWFNNFDSA-UHFFFAOYSA-N 2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-1-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]ethanone Chemical compound C1CN(CC2=NNN=C21)CC(=O)N3CCN(CC3)C4=CN=C(N=C4)NCC5=CC(=CC=C5)OC(F)(F)F LDXJRKWFNNFDSA-UHFFFAOYSA-N 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000010849 combustible waste Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Classifications
-
- 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
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/442—Wood or forestry waste
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- 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
-
- 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
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Ecology (AREA)
- Forests & Forestry (AREA)
- Wood Science & Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
본 발명은 혼합폐기물을 이용한 고형연료 및 이것의 제조방법에 대한 것으로, 특히 폐목재를 주원료로 하면서, 혼합폐비닐, 하수 및 분뇨슬러지를 혼합하여 생산량과 생산속도가 우수할 뿐만 아니라, 수분과 회분 함량은 낮으면서, 가연분 함량은 높고, 발열량도 현저히 높은 고형연료에 대한 것이다.
The present invention relates to a solid fuel using mixed waste and a method for producing the solid fuel, and more particularly, to a method for producing solid fuel using mixed waste and a method for producing the solid fuel using blended waste vinyl, sewage and manure sludge, It is for a solid fuel with a low content, a high amount of combustible components, and a significantly high calorific value.
일반적으로, 산림청에서 주기적으로 실시하는 간벌작업, 건물 철거에 따른 폐목자재 및 폐가구류 등에서 폐목재가 발생되는데, 이를 부분적이지만 톱밥 등으로 가공하여 재활용하기도 하지만 대부분 소각 등의 중간처리로 인하여 2차적인 환경오염을 유발시키는 등의 문제가 있다.Generally, waste wood is generated in the forestry office periodically by thinning work, waste materials from the demolition of building, and waste wood furniture. It is partially recycled by processing with sawdust, etc. However, Thereby causing environmental pollution.
또한, 혼합 폐비닐 등은 열용융공정과 압출공정 등을 거쳐서 재생하거나 소각장에서 소각 폐기하게 되는데, 이러한 비닐류의 재생품은 결국 2차적인 환경오염 즉, 연소시 다이옥신 등과 같은 발암물질을 발생시키게 된다.In addition, the mixed waste vinyl is regenerated through a heat melting process and an extrusion process, or incinerated at an incineration plant. Such a vinyl recycled product eventually generates secondary environmental pollutants, ie, carcinogens such as dioxin when burned.
이에 따라, 상기한 폐기물들을 이용하거나 서로 혼합하여 고형연료로 제조하는 다수의 기술이 등장하였다. Accordingly, a number of techniques have been developed for producing solid fuel using the above-mentioned wastes or mixing them with each other.
그러나, 수분, 회분, 가연분 등의 3성분 함량과 발열량 등의 물적 특성이 전혀 다른 다양한 종류의 폐기물을 어떠한 비율로 혼합해서 사용할 때, 가장 효과적이면서 효율적인지에 대한 체계적인 연구는 아직까지 이루어진 바가 없다.
However, no systematic studies have been conducted on the most effective and efficient methods for mixing various kinds of wastes having different physical properties such as moisture content, ash content, and combustible content, in terms of the ratio .
본 발명은 상기한 문제점을 해결하기 위한 것으로, 폐목재, 혼합폐비닐, 하수 및 분뇨슬러지를 이용하여 고형연료를 제조함에 있어서, 폐목재(폐목분, 톱밥, 우드칩(WCF) 순수폐목 및/또는 임목)를 주요 대상물로 하여 혼합폐비닐, 하수 및 분뇨슬러지의 함량을 최적화하고, 고형연료 제조를 위한 고형화 온도, 시간 및 성형압력을 최적화하기 위한 것이다. 즉, 본 발명은 생산량과 생산속도가 우수할 뿐만 아니라, 수분과 회분 함량은 낮으면서, 가연분 함량은 높고, 발열량도 현저히 높은 고형연료를 제조하는 것이 목적이다. Disclosure of Invention Technical Problem [8] Accordingly, the present invention has been made in view of the above problems, and an object of the present invention is to provide a method for producing solid fuel using waste wood, mixed waste vinyl, sewage and manure sludge, waste wood (waste wood, sawdust, wood chip (WCF) Or timber) as a main object to optimize the content of mixed waste vinyl, sewage and manure sludge, and to optimize solidification temperature, time and molding pressure for solid fuel production. That is, the object of the present invention is to produce a solid fuel which is excellent in productivity and production rate, has a low moisture and ash content, a high amount of combustible components, and a remarkably high calorific value.
또한, 본 발명은 유해물질의 함량을 낮출 수 있고, 성형제품으로써의 물적 특성이 양호한 고형연료를 제공하기 위한 것이다.
Further, the present invention is to provide a solid fuel which can lower the content of harmful substances and has good physical properties as a molded product.
상기한 목적을 달성하기 위한 본 발명에 따른 폐기물을 이용한 고형연료는, 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및 임목으로 이루어진 군에서 하나 이상이 선택된 제1연료조성물 15~99중량%과, 파쇄하고 분쇄시킨 혼합폐비닐 또는 건조 파쇄한 하수 및 분뇨슬러지에서 하나 이상이 선택된 제2연료조성물 1~85중량%이 혼합되어 이루어진 것이다. To achieve the above object, the solid fuel using waste according to the present invention comprises 15 to 99% by weight of a first fuel composition selected from the group consisting of wood pulp, sawdust, pure wood pulp (WCF) , 1 to 85% by weight of a second fuel composition selected from one or more of crushed and pulverized mixed waste vinyl or dry crushed sewage and manure sludge.
여기서, 상기 제1연료조성물은 20~80중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~80중량%인 것일 수 있다. Here, the first fuel composition may be 20 to 80 wt%, and the second fuel composition may be 20 to 80 wt% of mixed waste vinyl.
그리고, 상기 제1연료조성물은 20~50중량%이고, 상기 제2연료조성물은 혼합폐비닐20~40중량%과 하수및분뇨슬러지 30~40중량%인 것이 바람직하다. It is preferable that the first fuel composition is 20 to 50 wt%, the second fuel composition is 20 to 40 wt% of mixed waste vinyl, and 30 to 40 wt% of sewage and manure sludge.
또한, 상기 제2연료조성물은 물품 포장재로 사용되었던 폐비닐을 100mmㅧ100mm 크기 이하로 파쇄하고 분쇄시킨 것이 바람직하다. Also, it is preferable that the second fuel composition is pulverized and pulverized waste vinyl which has been used as an article packaging material to have a size of 100 mm ㅧ 100 mm or less.
또한, 상기 제2연료조성물은 하수처리장 및 축산분뇨처리장에서 발생되는 슬러지를 건조, 파쇄시킨 것이 바람직하다.
In addition, the second fuel composition is preferably dried and crushed in sludge generated in a sewage treatment plant and an animal manure treatment plant.
한편, 본 발명의 다른 실시형태는, 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및 임목으로 이루어진 군에서 하나 이상이 선택된 제1연료조성물을 준비하는 단계; 파쇄하고 분쇄시킨 혼합폐비닐 또는 건조 파쇄한 하수 및 분뇨슬러지에서 하나 이상 선택된 제2연료조성물을 준비하는 단계; 및 상기 제1연료조성물 15~99중량%와 제2연료조성물 1~85중량%를 혼합한 혼합물을 성형하는 단계;를 포함하는 폐기물을 이용한 고형연료의 제조방법일 수 있다.On the other hand, another embodiment of the present invention is a method for producing a fuel composition, comprising: preparing a first fuel composition selected from the group consisting of wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood pulp; Preparing a second fuel composition selected from one or more of crushed and pulverized mixed waste vinyl or dry crushed sewage and manure sludge; And forming a mixture of 15 to 99% by weight of the first fuel composition and 1 to 85% by weight of the second fuel composition.
여기서, 상기 제1연료조성물과 제2연료조성물을 혼합하는 것은, 상기 제1연료조성물은 20~80중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~80중량%인 것일 수 있다. Here, mixing the first fuel composition and the second fuel composition may be such that the first fuel composition is 20-80 wt% and the second fuel composition is 20-80 wt% mixed waste vinyl.
그리고, 상기 제1연료조성물은 20~50중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~40중량%과 하수 및 분뇨슬러지 30~40중량%인 것이 바람직하다. It is preferable that the first fuel composition is 20 to 50 wt%, the second fuel composition is 20 to 40 wt% of mixed waste vinyl, and 30 to 40 wt% of sewage and manure sludge.
그리고, 상기 제2연료조성물을 준비하는 단계는, 상기 혼합폐비닐을 파쇄한 후 자력 선별기로 금속성분을 1차 제거하는 단계; 상기 금속성분을 1차 제거한 혼합폐비닐을 풍력 선별기를 통해 비중이 0.1이하인 것만을 선별하는 단계; 및 상기 선별한 혼합폐비닐을 분쇄한 후 자력 선별기로 금속성분을 2차 제거하는 단계;를 포함하는 것이 가능하다.
The step of preparing the second fuel composition may include a step of firstly removing metal components by a magnetic separator after crushing the mixed waste vinyl; Selecting a mixed waste vinyl material having a specific gravity of 0.1 or less through a wind separator; And a step of secondarily removing the metal component with the magnetic separator after the pulverized mixed waste vinyl is pulverized.
또한, 본 발명은 상기한 제조방법에 의해 제조되어, 상기 제1연료조성물은 20~80중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~80중량%가 혼합되어 이루어지거나, 상기 제1연료조성물은 20~50중량%이고, 상기 제2연료조성물은 혼합폐비닐20~40중량%과 하수 및 분뇨슬러지 30~40중량%가 혼합되어 이루어진 것을 특징으로 하는 폐기물을 이용한 고형연료인 것도 가능하다.
Also, the present invention is produced by the above-described production method, wherein the first fuel composition is 20 to 80 wt%, the second fuel composition is a mixture of 20 to 80 wt% of mixed waste vinyl, Wherein the fuel composition is 20 to 50 wt% and the second fuel composition is a mixture of 20 to 40 wt% of mixed waste vinyl and 30 to 40 wt% of sewage and manure sludge. Do.
기타 실시예들의 구체적인 사항들은 상세한 설명 및 도면들에 포함되어 있다.
The details of other embodiments are included in the detailed description and drawings.
이러한 본 발명은 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및/또는 임목, 혼합폐비닐 또는 하수 및 분뇨슬러지의 함량을 최적화하고, 고형연료 제조를 위한 고형화 온도, 시간 및 성형압력을 최적화함으로써, 생산량과 생산속도가 우수할 뿐만 아니라, 수분과 회분 함량은 낮으면서, 가연분 함량은 높고, 발열량도 현저히 높은 고형연료를 제조할 수 있는 효과가 있다. This invention can be used to optimize the content of waste wood powder, sawdust, wood chip (WCF) pure wood waste and / or wood, mixed waste vinyl or sewage and manure sludge and optimize solidification temperature, time and molding pressure for solid fuel production , It has an effect of producing a solid fuel which is excellent in production amount and production speed, has a low moisture and ash content, has a high amount of combustible components, and has a remarkably high calorific value.
또한, 본 발명은 폐기물 원료의 파쇄 및 분쇄 과정 중에, 자력 선별기로 금속성분을 제거하여 유해물질의 함량을 낮출 수 있고, 풍력 선별기로 비중이 낮은 원료만을 선별하여 이용함으로써 성형제품으로써의 물적 특성이 양호한 고형연료를 제공할 수 있는 것이다.
In addition, the present invention can reduce the content of harmful substances by removing metal components by a magnetic separator during the crushing and pulverizing process of waste materials, and by selecting only raw materials having low specific gravity as a wind separator, It is possible to provide a good solid fuel.
도 1은 본 발명의 일 실시예에 따른 고형연료 성형장치와 이를 구성하는 판넬, 감속기 및 모터, 다이스, 투입호퍼를 나타내는 사진이고,
도 2는 본 발명에 따라 복합 고형연료 제조공정에서 슬러지류를 정량적으로 공급하기 위한 정량투입장치의 일례를 나타내는 사진이고,
도 3은 본 발명의 일 실시예에 따른 고형연료의 제조방법과 복합고형연료 전처리 방법의 순서를 나타내는 흐름도이고,
도 4 내지 도 6은 본 발명의 일례에 따라 제조된 폐목재류 혼합시료의 고형연료 성형물을 나타내는 사진이고,
도 7은 본 발명의 일례에 따라 제조된 슬러지/폐목분 혼합시료의 고형연료 성형물을 나타내는 사진이다.1 is a photograph showing a solid fuel forming apparatus according to an embodiment of the present invention and a panel, a speed reducer, a motor, a dice, and a loading hopper constituting the same,
FIG. 2 is a photograph showing an example of a metering device for quantitatively supplying sludge in a process for producing a complex solid fuel according to the present invention,
3 is a flowchart showing a procedure of a solid fuel production method and a composite solid fuel pretreatment method according to an embodiment of the present invention,
FIGS. 4 to 6 are photographs showing a solid fuel molding of a waste wood mixed sample produced according to an example of the present invention,
7 is a photograph showing a solid fuel molding of a sludge / waste wood particle mixed sample produced according to an example of the present invention.
본 발명은 다양한 변환을 가할 수 있고 여러 가지 실시 예를 가질 수 있는 바, 특정 실시 예들을 도면에 예시하고 상세한 설명에서 상세하게 설명하고자 한다. 그러나, 이는 본 발명을 특정한 실시 형태에 대해 한정하려는 것이 아니며, 본 발명의 사상 및 기술 범위에 포함되는 모든 변환, 균등물 내지 대체물을 포함하는 것으로 이해되어야 한다. 본 발명을 설명함에 있어서 관련된 공지 기술에 대한 구체적인 설명이 본 발명의 요지를 흐릴 수 있다고 판단되는 경우 그 상세한 설명을 생략한다.BRIEF DESCRIPTION OF THE DRAWINGS The present invention is capable of various modifications and various embodiments, and specific embodiments are illustrated in the drawings and will be described in detail in the detailed description. It is to be understood, however, that the invention is not to be limited to the specific embodiments, but includes all modifications, equivalents, and alternatives falling within the spirit and scope of the invention. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
본 출원에서 사용한 용어는 단지 특정한 실시예를 설명하기 위해 사용된 것으로, 본 발명을 한정하려는 의도가 아니다. 단수의 표현은 문맥상 명백하게 다르게 뜻하지 않는 한, 복수의 표현을 포함한다. 본 출원에서, "포함하다" 또는 "가지다" 등의 용어는 명세서상에 기재된 특징, 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것이 존재함을 지정하려는 것이지, 하나 또는 그 이상의 다른 특징들이나 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것들의 존재 또는 부가 가능성을 미리 배제하지 않는 것으로 이해되어야 한다.The terminology used in this application is used only to describe a specific embodiment and is not intended to limit the invention. The singular expressions include plural expressions unless the context clearly dictates otherwise. In the present application, the terms "comprises" or "having" and the like are used to specify that there is a feature, a number, a step, an operation, an element, a component or a combination thereof described in the specification, But do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, or combinations thereof.
제1, 제2 등의 용어는 다양한 구성요소들을 설명하는데 사용될 수 있지만, 상기 구성요소들은 상기 용어들에 의해 한정되어서는 안 된다. 상기 용어들은 하나의 구성요소를 다른 구성요소로부터 구별하는 목적으로만 사용된다.
The terms first, second, etc. may be used to describe various components, but the components should not be limited by the terms. The terms are used only for the purpose of distinguishing one component from another.
본 발명은 폐기물을 이용한 고형연료에 대한 것이다. 그 중에서도, 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및/또는 임목, 발열량이 높은 폐비닐류, 폐기물 용량이 많으면서 쉽게 구입할 수 있는 하수 및 분뇨슬러지를 사용하는 것이다. The present invention is directed to a solid fuel using waste. Among them, waste wood pulp, sawdust, pure wood pulp and wood chips (WCF) and / or timber, high calorific waste vinyl waste, sewage and manure sludge which are readily available with high waste capacity are used.
본 발명자들은 상기한 원료의 조성과 함량을 서로 다르게 하여 고형연료 시료를 제조하고, 성형 온도, 시간, 압력을 서로 다르게 하여 고형연료를 제조하고, 이에 대한 실험을 거듭한 결과, 상기 조성 및 함량에 따라 고형연료의 생산량과 생산속도, 그리고 수분, 회분 및 가연분의 함량과, 발열량에서 큰 차이가 있음을 알게 되었으며, 이 과정에서 상기 조성 및 함량을 최적화와 고형화 온도, 시간 및 압력을 최적화함으로써 본 발명을 완성하였다.The present inventors produced a solid fuel sample by making the composition and the content of the raw materials different from each other, and made solid fuel by making the molding temperature, time, and pressure different from each other. As a result of repeated experiments, It was found that there is a large difference in the amount of production of solid fuel, production rate, moisture, ash and flammable content, and calorific value. In this process, optimization of the composition and content and optimization of solidification temperature, Thereby completing the invention.
이에 따른 본 발명은 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및 임목으로 이루어진 군에서 하나 이상이 선택된 제1연료조성물은 20~80중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~80중량%가 혼합되어 이루어지거나, 또는 제1연료조성물은 20~50중량%이고, 상기 제2연료조성물은 혼합폐비닐 20~40중량%과 하수 및 분뇨슬러지 30~40중량%가 혼합되어 이루어진 폐기물을 이용한 고형연료이다. Accordingly, the first fuel composition is selected from the group consisting of wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood, and the first fuel composition is 20-80 wt% Or the first fuel composition is 20 to 50 wt%, and the second fuel composition is a mixture of 20 to 40 wt% of mixed waste vinyl and 30 to 40 wt% of sewage and manure sludge It is a solid fuel using waste.
또한, 상기 제2연료조성물은 물품 포장재로 사용되었던 폐비닐을 100mmㅧ100mm 크기 이하로 파쇄하고 분쇄시킨 것이 바람직한데, 상기 물품 포장재로 사용되었던 폐비닐이 폐합성수지나 농촌에서 버려지는 폐비닐류에 비하여 수분함량이 낮으면서도 발열량이 높으며, 크기가 작은 것이 제1연료조성물과의 혼합에 적합하다.The second fuel composition is preferably pulverized and ground to a size of 100 mm ㅧ 100 mm or less, which was used as an article packaging material. Compared with the waste vinyl used in the waste packaging material or the waste vinyl in the rural area, The amount of heat generated is low while the water content is low, and a small size is suitable for mixing with the first fuel composition.
나아가, 상기 제1연료조성물로써 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및/또는 임목 등은 각각 서로 다른 3성분(수분, 회분, 가연분) 함량과 발열량 등의 물적 특성을 가지는 바, 후술하는 실시예에 나타난 바와 같이 제2연료조성물과 혼합됨에 있어서 서로 다른 함량으로 포함되는 것이 더욱 바람직하다. Further, as the first fuel composition, waste wood powder, sawdust, pure wood waste wood (WCF) and / or timber have physical properties such as three different components (moisture, ash, and combustible) It is more preferable that they are contained in different contents in mixing with the second fuel composition as shown in the following examples.
한편, 본 발명의 다른 실시형태는, 폐비닐이나 폐합성수지를 파쇄하고 분쇄시켜서 제1연료조성물을 준비하는 단계(S10); 슬러지, 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및 임목으로 이루어진 군에서 하나 이상이 선택된 제1연료조성물을 준비하는 단계(S20); 및 상기 제1연료조성물 20~80중량%과 제2연료조성물 혼합폐비닐 20~80중량%가 혼합, 또는 제1연료조성물 20~50중량%과 제2연료조성물 혼합폐비닐20~40중량%과 하수및분뇨슬러지 30~40중량%을 혼합한 혼합물을 성형하는 단계(S30);를 포함하는 폐기물을 이용한 고형연료의 제조방법일 수 있다.According to another embodiment of the present invention, there is provided a method of manufacturing a fuel cell, comprising: (S10) preparing a first fuel composition by crushing and crushing waste vinyl or waste synthetic resin; Preparing (S20) a first fuel composition selected from the group consisting of sludge, waste wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood; And 20 to 80% by weight of the first fuel composition and 20 to 80% by weight of the second fuel composition mixed waste vinyl, or 20 to 50% by weight of the first fuel composition and 20 to 40% And 30 to 40 wt% of sewage and manure sludge (S30). The solid fuel may be produced by using the waste.
상기 제2연료조성물로써 혼합폐비닐이나 하수 및 분뇨슬러지를 파쇄하고 분쇄시키는 방법 및 크기는 특별히 제한되지 않고, 이 기술분야에 널리 알려진 다양한 형태의 파쇄기와 분쇄기를 이용할 수 있다. There are no particular limitations on the size and the method of crushing and pulverizing mixed waste vinyl and sewage and manure sludge with the second fuel composition, and various types of crushers and crushers known in the art can be used.
그리고, 상기 제1연료조성물로써 슬러지, 폐목분, 톱밥, 우드칩(WCF) 순수폐목 및 임목 역시 이 기술분야에 널리 알려진 다양한 형태의 것을 모두 포함한다. 이에 대해서는, 후술하는 실시예에서 상세하게 설명한다. As the first fuel composition, sludge, wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood pulp are all included in various forms well known in the art. This will be described in detail in the following embodiments.
본 발명은 제1연료조성물 20~80중량%과 제2연료조성물 혼합폐비닐 20~80중량%를 혼합, 또는 제1연료조성물 20~50중량%과 제2연료조성물 혼합폐비닐 20~40중량%과 하수 및 분뇨슬러지 30~40중량%을 혼합하여 혼합물을 얻는 것이 특징이다. 이와 같은 혼합비율로 혼합된 혼합물을 이용하여 고형연료를 제조하면, 생산량과 생산속도가 우수할 뿐만 아니라, 수분과 회분 함량은 낮으면서, 가연분 함량은 높고, 발열량도 현저히 높은 고형연료를 제조할 수 있다. The present invention relates to a fuel composition comprising 20 to 80% by weight of a first fuel composition and 20 to 80% by weight of a second fuel composition mixed waste vinyl, or 20 to 50% by weight of a first fuel composition and 20 to 40 %, Sewage and manure sludge of 30 to 40% by weight to obtain a mixture. When a solid fuel is produced using such a mixture at such a mixing ratio, a solid fuel having a high production amount and a high production rate, a low moisture and ash content, a high amount of combustible matter, and a remarkably high calorific value can be produced .
이러한 혼합물을 고형연료로 성형하는 방법이나 장치는 특별히 제한되지 않고, 이 기술분야에서 알려진 다양한 것을 모두 포함하며, 제조된 고형연료의 형상 또한 특별히 제한되지 않는다. The method or apparatus for molding such a mixture into a solid fuel is not particularly limited and includes all of various things known in the art, and the shape of the produced solid fuel is also not particularly limited.
특별히, 본 발명에서 상기 제2연료조성물을 준비하는 단계(S10)는, 상기 복합폐비닐을 파쇄한 후 자력 선별기로 금속성분을 1차 제거하는 단계(S12); 상기 금속성분을 1차 제거한 폐비닐이나 폐합성수지를 풍력 선별기를 통해 비중이 0.1이하인 것만을 선별하는 단계(S14); 및 상기 선별한 복합 폐비닐을 분쇄한 후 자력 선별기로 금속성분을 2차 제거하는 단계(S16);를 포함하는 것이 바람직하다. 이러한 본 발명은 폐기물 원료의 파쇄 및 분쇄 과정 중에, 자력 선별기로 금속성분을 제거하여 유해물질의 함량을 낮출 수 있고, 풍력 선별기로 비중이 낮은 원료만을 선별하여 이용함으로써 성형제품으로써의 물적 특성이 양호한 고형연료를 제조할 수 있는 것이다.
Specifically, the step (S10) of preparing the second fuel composition according to the present invention comprises: (S12) a step of removing the metal component by a magnetic separator after the compound waste vinyl is crushed; (S14) selecting only waste vinyl or waste synthetic resin having a specific gravity of 0.1 or less through a wind separator; And a step (S16) of secondarily removing metal components by the magnetic separator after pulverizing the selected composite waste vinyl. The present invention can reduce the content of harmful substances by removing metal components by using a magnetic separator during the crushing and pulverizing process of waste materials, and by selecting only raw materials having low specific gravity as a wind separator, It is possible to produce a solid fuel.
또한, 본 발명은 상기한 제조방법에 의해 제조되어, 상기 제1연료조성물 20~80중량%과 제2연료조성물 혼합폐비닐 20~40중량%를 혼합, 또는 제1연료조성물 20~50중량%과 제2연료조성물 혼합폐비닐 20~40중량%과 하수 및 분뇨슬러지 30~40중량%을 혼합되어 이루어진 것을 특징으로 하는 폐기물을 이용한 고형연료인 것도 가능하다. Also, the present invention provides a fuel composition comprising 20 to 80% by weight of the first fuel composition and 20 to 40% by weight of the second fuel composition mixed waste vinyl, or 20 to 50% by weight of the first fuel composition, 20 to 40% by weight of the second fuel composition mixed waste vinyl, and 30 to 40% by weight of sewage and manure sludge.
이러한 본 발명은 폐목재, 혼합폐비닐, 하수 및 분뇨슬러지를 이용하여 고형연료를 제조함에 있어서, 폐목재(폐목분, 톱밥, 우드칩(WCF) 순수폐목 및/또는 임목)를 주요 대상물로 하여 혼합폐비닐, 하수 및 분뇨슬러지의 함량을 최적화하고, 고형연료 제조를 위한 고형화 온도, 시간 및 성형압력이 최적화됨으로써, 생산량과 생산속도가 우수할 뿐만 아니라, 수분과 회분 함량은 낮으면서, 가연분 함량은 높고, 발열량도 현저히 높은 고형연료를 제조할 수 있는 효과가 있다.
The present invention relates to a method of producing a solid fuel using waste wood, mixed waste vinyl, sewage and manure sludge, and using waste wood (waste wood, sawdust, wood chip (WCF) pure wood waste and / By optimizing the content of mixed waste vinyl, sewage and manure sludge and by optimizing the solidification temperature, time and molding pressure for solid fuel production, not only is it superior in yield and production rate, but also in moisture and ash content, The solid fuel having a high content and a significantly high calorific value can be produced.
본 발명은 하기의 실시예에 의하여 보다 더 잘 이해 될 수 있으며, 하기의 실시예는 본 발명의 예시 목적을 위한 것이며, 첨부된 특허청구범위에 의하여 한정되는 보호범위를 제한하고자 하는 것은 아니다.
The present invention may be better understood by the following examples, which are for the purpose of illustrating the invention and are not intended to limit the scope of protection defined by the appended claims.
실시예 1: 시료의 준비Example 1: Preparation of sample
본 실시예에서는 폐목재류, 폐합성수지, 하수 및 분뇨슬러지의 혼합 및 성형테스트를 수행하기 위해서, 산업공정에서 대량으로 발생되고 취급이 용이한 폐기물을 본 실험의 성형대상으로 선정하였다. In this embodiment, in order to carry out the mixing and molding test of waste wood, waste synthetic resin, sewage and manure sludge, wastes generated in a large amount in the industrial process and easy to handle are selected as the objects to be molded in this experiment.
선정한 대상시료는 고형연료 성형시 주재료로 사용할 폐목재 5종(목분, 톱밥, 폐목, WCF, 임목), 혼합 폐비닐류, 하수 및 분뇨슬러지을 혼합재료로서 단물질 및 혼합물질의 성형테스트를 위해 공정중에 직접 샘플링하여 가장 대표성을 띄는 지점 및 시점에 시료를 샘플링하였다. The selected samples are used for the molding test of single substances and mixed materials as mixed materials of 5 types of waste wood (wood, sawdust, waste wood, WCF, wood), mixed waste vinyl, sewage and manure sludge to be used as main material in solid fuel molding The samples were directly sampled and sampled at the most representative points and time points.
선정된 대상시료에 대해 시료별 형태와 상태를 <표 1> 에 정리하였다. Table 1 summarizes the form and status of the selected samples for each sample.
(혼합)Waste vinyl
(mix)
*비닐 내부에 유기성 폐기물(음식물, 협잡물 등)이 묻어서 배출되 악취 유발
*압축상태로 반임됨* Mostly plastic packaging material
* Organic waste (food, dirt, etc.) is deposited inside the plastic, and it is emitted.
* Compressed state
*점성이 높으며 악취가 남* High moisture content
* High viscosity and odor
*입자가 작아 혼합에 유리함
*제품 생산 후 폐기되는 것으로 재활용시 타 폐목재류에 비해 부가가치가 있음.* Residues after crushing of wood
* Particle size is small and it is advantageous for mixing.
* It is discarded after production, so there is added value when recycled compared to other timber.
*제품으로 톤당 6만원으로 판매됨* Shredded residue of wood
* Sold as 60,000 won per ton
*페인트 등의 유기용제류가 혼합된 형태* Shredding residues of upholstery
* Mixture of organic solvent such as paint
*소각로 등에 직접 투입이 가능함* Wood waste
* Can be directly injected into incinerator
*나뭇가지의 형태가 다량 함유되어있음* Pure wood is big in size
* Contains a large amount of tree branches.
실시예 2: 제조장치Example 2: Manufacturing apparatus
본 발명의 복합고형연료 성형테스트에는 복합고형연료 제조공정의 전처리부(1차 파쇄 - 2차 파쇄 - 풍력선별 - 분쇄)와 Screw dies type의 성형장치(외부공급)로 구성되어 있으며 자세한 구성은 아래와 같다.The composite solid fuel forming test according to the present invention comprises a pretreatment unit (primary crushing - secondary crushing - wind power sorting - crushing) and a screw dies type crushing unit (external supply) of a composite solid fuel production process. same.
* RPF 성형장치(Screw dies type)* RPF molding device (Screw dies type)
본 실험에서는 폐기물 반입에서 분쇄공정까지의 절차(1차 파쇄 - 2차 파쇄 - 풍력선별 - 분쇄)를 통해 대상시료의 전처리를 하였고, 성형은 외부에서 공급된 스크류다이즈 방식의 2ton/day 처리용량의 성형장치를 이용하였다. In this experiment, the sample was pretreated through the procedure from the waste transfer to the pulverizing process (primary pulverization - secondary pulverization - wind power sorting - pulverization), and the molding was carried out using a 2 ton / day treatment capacity Was used.
도 1에는 이러한 고형연료 성형장치와 이를 구성하는 판넬, 감속기 및 모터, 다이스, 투입호퍼를 나타내고 있으며, 상세한 사양은 하기 표 2에 기재된 바와 같다. FIG. 1 shows such a solid fuel molding apparatus, and a panel, a speed reducer, a motor, a dice, and a hopper constituting the same, and detailed specifications are as shown in Table 2 below.
(압축가열성형)Screw dies
(Compression molding)
* 슬러지/폐기물 정량투입장치* Sludge / waste dosing device
도 2 및 하기 표 3에 나타난 정량투입장치는 복합고형연료 제조공정에서 슬러지류를 정량적으로 공급하는 장치로서, 폐기물 분배장치와 연계하여 슬러지/폐기물을 혼합시키고, 성형장치로 투입되는 컨베이어에 안정적으로 이송시키는 역할을 한다. The dosing device shown in FIG. 2 and the following Table 3 is a device for quantitatively supplying sludge in a process of producing a solid fuel, and it mixes sludge / waste in connection with a waste distribution device, It is also responsible for transferring.
*모터 : 3HP, 정역회전, 속도제어 * Type: Screw type
* Motor: 3HP, reverse rotation, speed control
*운반 용량 : 1/h
*모 터 : 3HP, 정회전, 속도제어* Type: Screw type
* Carrying capacity: 1 / h
* Motor: 3HP, forward rotation, speed control
실시예 3: 제조방법Example 3: Preparation method
도 3은 본 발명의 일 실시예에 따른 고형연료의 제조방법과 복합고형연료(가연성폐기물 + 슬러지류) 전처리 방법의 순서를 나타내는 흐름도이다.3 is a flow chart showing the procedure of the solid fuel production method and the composite solid fuel (combustible waste + sludge flow) pretreatment method according to an embodiment of the present invention.
먼저, 대상 폐기물(혼합 폐비닐류)을 1차 파쇄기에서 파쇄선별한 후 2차 파쇄기를 거치면 폐기물은 200*200이하로 배출되고, 고정식 자력선별기를 거쳐 금속성분을 1차 제거하며, 풍력선별기에 투입한다. 그러면, 비중선별이 완료된 파쇄물은 2차 자력선별을 거쳐 분쇄기에 투입되며, 분쇄된 폐기물은 100*100이하로 배출되고, 배출부에 정량공급되는 슬러지와 혼합되게 된다. 혼합된 슬러지와 폐기물은 컨베이어로 이송되어 성형장치로 투입된 후 성형된 복합고형연료제품으로 배출된다.
First, when the target waste (mixed waste vinyl) is crushed in a primary crusher and then passed through a secondary crusher, the waste is discharged to 200 * 200 or lower, and the metal components are firstly removed through a fixed magnetic separator, do. Then, the crushed waste is discharged to 100 * 100 or less, and mixed with the sludge to be supplied to the discharge part in a fixed amount. The mixed sludge and wastes are transferred to a conveyor, fed into a molding machine, and then discharged into a molded composite solid fuel product.
실시예 4: 고형연료의 제조Example 4: Preparation of solid fuel
본 발명에 따라 복합고형연료 성형실험에 사용한 주재료는 폐목재 5종(목분, 톱밥, 폐목, WCF, 임목), 혼합 폐비닐류, 하수 및 분뇨슬러지를 혼합하여 고형연료제품으로 제조하였다. 폐목재류를 이용한 단일물질 성형 실험은 표 4에 나타난 바와 같다. According to the present invention, the main material used in the complex solid fuel molding experiment was prepared as a solid fuel product by mixing 5 kinds of waste wood (wood powder, sawdust, wood pulp, WCF, wood), mixed waste vinyl, sewage and manure sludge. Table 4 shows the results of single-material molding experiments using waste wood.
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
대상시료의 주요 분석은 아래 표 5과 같이 원시료와 고형연료제품에 해당하는 성상분석 항목을 선정하여 기준에 따라 물성 및 제품평가를 수행하였다. For the main analysis of the target samples, the property analysis and the product evaluation were performed according to the criteria by selecting the property analysis items corresponding to the raw and solid fuel products as shown in Table 5 below.
실험예 1: 원시료의 물성분석Experimental Example 1: Analysis of Physical Properties of Raw Samples
본 발명에 따른 복합고형연료제품 제조를 위해 폐목재 5종(목분, 톱밥, 폐목, WCF, 임목), 혼합 폐비닐류, 하수 및 분뇨슬러지를 선정하여 실험을 수행하였다. 대상 시료의 특성은 상기 표 1에 나타난 바와 같고, 하기 표 6 및 표 7에서는 원시료의 삼성분, 발열량 및 비중을 분석하여 그 값을 나타내었다. For the production of the composite solid fuel product according to the present invention, five types of waste wood (wood, sawdust, wood waste, WCF, wood), mixed waste vinyl, sewage and manure sludge were selected and tested. The properties of the samples are shown in Table 1, and Tables 6 and 7 show the values of the ternary amounts, calories and specific gravity of the raw materials.
(Three-
component)Proximate Analysis
(Three-
component)
실험예 2: Screw dies type 성형장치 생산량 및 수율Experimental Example 2: Screw dies type molding apparatus production amount and yield
본 실험에서는 성형장치의 생산량과 수율을 조사하기 위해 주성형물, 슬러지/폐목분, 기타 목분류 및 혼합시료 3가지로 구분하여 테스트를 진행하였다. 성형시작시 운전온도는 각각 180℃로 설정 후 진행하였다.In order to investigate the yield and yield of the molding machine, the test was divided into three types: main molding, sludge / waste wood, other neck classification and mixed sample. The operation temperature at the start of molding was set to 180 ° C and then proceeded.
하기 표 8에 나타난 바와 같이, 주요 성형물 테스트에는 복합비닐류를 적용하였고 생산속도는 0.42 ton/hr, 81.48 %의 수율을 얻었다. 슬러지와 폐목분에 대한 테스트에서는 0.52 ton/hr의 생산속도와 76.47%의 수율을 얻었으며, 기타 폐목분류와 혼합시료테스트에서는 0.53 ton/hr의 생산속도와 81.25% 수율을 얻었다. As shown in Table 8 below, composite vils were applied to the main mold test and the production rate was 0.42 ton / hr and 81.48% yield. The sludge and waste wood samples showed a yield of 0.52 ton / hr and a yield of 76.47%. Other wood waste and mixed sample tests yielded a yield of 0.53 ton / hr and a yield of 81.25%.
(kg)input
(kg)
(분['])Injection time
(minute['])
(kg/hr)Feed rate
(kg / hr)
(kg)output
(kg)
(kg/hr)Production speed
(kg / hr)
(%)yield
(%)
3가지 운전조건에 대한 고형연료 생산속도는, 주 성형물 테스트에서 폐비닐류에 포함된 수분량이 많아 생산속도와 수율에 영향을 준 것으로 판단되며, 슬러지와 폐목분에 대한 테스트에서는 0.52 ton/hr로 높았고, 기타 폐목분류와 혼합시료 테스트에서는 0.53 ton/hr로 더 높았다.
The solid fuel production rate for the three operating conditions was considered to have affected the production rate and yield due to the high water content of the waste vinyl in the main molding test and 0.52 ton / hr in the test for sludge and waste wood powder And 0.53 ton / hr in other waste wood classification and mixed sample test.
실험예 3: 고형연료제품 생산Experimental Example 3: Production of solid fuel products
실험예 3-1 : 주 재료 단일 성형 실험Experimental Example 3-1: Single Molding Experiment of Main Material
본 실험에서는 주요 성형재료로 사용될 폐목재에 대해 실험을 수행하였고, 성형시작시 운전온도는 각각 160℃로 설정 후 진행하였다. 3종의 성형물에 대한 고형연료 생산속도는 평균 0.42 ton/hr 로 상당히 낮은 성능을 보였다. Experiments were performed on waste wood to be used as a main molding material in this experiment, and the operation temperature was set at 160 ° C at the start of molding. The solid fuel production rate for the three types of moldings was 0.42 ton / hr, which is considerably lower than that of the other three types.
본 발명에 따라 제조된 복합폐비닐 혼합시료의 고형연료 성형물을 나타내는 사진 및 물성분석 결과는 하기 표 9에 나타난 바와 같다.The photographs and physical property analysis results of the solid fuel moldings of the mixed waste vinyl mixture samples prepared according to the present invention are shown in Table 9 below.
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
실험예 3-2 : 복합폐비닐류 혼합에 따른 성형실험EXPERIMENTAL EXAMPLE 3-2: Molding Experiment According to the Mixing of Compounded Vinyls
본 실험에서는 주원료인 폐목재류(폐목분, 톱밥, 폐목, WCF, 임목)에 복합폐비닐류를 혼합하여 실험을 수행하였고 성형시작시 운전온도는 각각 160℃로 설정 후 진행하였다. 폐목재류 성형물에 대한 고형연료 생산속도는 평균 0.52 ton/hr로 높은 편이었다.In this experiment, mixed waste vinyls were mixed with waste wood (pulpwood, sawdust, wood pulp, WCF, wood) which is the main raw material, and the operation temperature was set to 160 ° C at the start of molding. The solid fuel production rate for waste wood products was as high as 0.52 ton / hr on average.
본 발명에 따라 제조된 복합폐비닐 혼합시료의 고형연료 성형물을 나타내는 사진 및 물성분석 결과는 하기 표 10~12에 나타난 바와 같다.Photographs and physical property analysis results of the solid fuel moldings of the mixed waste vinyl mixed samples produced according to the present invention are shown in Tables 10 to 12 below.
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
실험예 3-3 : 복합폐비닐류/하수 및 분뇨슬러지 혼합에 따른 성형실험Experimental Example 3-3: Molding Experiment According to Mixed Waste Vinyl / Sewage and Poultry Sludge Mixing
본 실험에서는 폐목재류에 하수 및 분뇨슬러지를 15~35% 그리고 복합폐비닐류를 30~70% 를 혼합하여 실험을 수행하였고 성형시작시 운전온도는 각각 180℃로 설정 후 진행하였다. In this experiment, 15 ~ 35% of sewage and manure sludge were mixed with 30 ~ 70% of mixed waste vinyl sludge, and the operation temperature was set to 180 ℃ at the start of molding.
본 발명에 따라 제조된 복합폐비닐/하수 및 분뇨슬러지 혼합시료의 고형연료 성형물을 나타내는 사진 및 물성분석 결과는 하기 표 13~14에 나타난 바와 같다.Photographs and physical property analysis results of the solid fuel moldings of the mixed waste vinyl / sewage and manure sludge mixture samples prepared according to the present invention are shown in Tables 13 to 14 below.
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
(℃)Temperature
(° C)
(min)time
(min)
(kgf/cm2)pressure
(kg f / cm 2)
(g/cm3)density
(g / cm 3)
(kcal/kg)Calorific value
(kcal / kg)
한편, 상기에서는 본 발명을 특정의 바람직한 실시예에 관련하여 도시하고 설명하였지만, 이하의 특허청구범위에 의해 마련되는 본 발명의 기술적 특징이나 분야를 이탈하지 않는 한도 내에서 본 발명이 다양하게 개조 및 변화될 수 있다는 것은 당업계에서 통상의 지식을 가진 자에게 명백한 것이다.
While the present invention has been particularly shown and described with reference to preferred embodiments thereof, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, It will be apparent to those skilled in the art that changes may be made.
Claims (7)
15 to 99% by weight of a first fuel composition selected from the group consisting of waste wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood pulp, and mixed pulverized vinyl pulverized or pulverized waste water and manure sludge 2 fuel composition comprising 1 to 85% by weight of a solid fuel.
상기 제1연료조성물은 폐목분 20~80중량%이고,
상기 제2연료조성물은 혼합폐비닐 20~80중량%인 것을 특징으로 하는 폐기물을 이용한 고형연료.
The method according to claim 1,
Wherein the first fuel composition comprises 20 to 80% by weight of waste wood,
Wherein the second fuel composition is 20 to 80 wt% mixed waste vinyl.
상기 제1연료조성물은 20~50중량%이고,
상기 제2연료조성물은 혼합폐비닐 20~40중량%과 하수및분뇨슬러지 30~40중량%인 것을 특징으로 하는 폐기물을 이용한 고형연료.
The method according to claim 1,
Wherein the first fuel composition is 20 to 50 wt%
Wherein said second fuel composition is 20-40 wt% mixed waste vinyl and 30-40 wt% sewage and manure sludge.
파쇄하고 분쇄시킨 혼합폐비닐 또는 건조 파쇄한 하수및분뇨슬러지에서 하나 이상 선택된 제2연료조성물을 준비하는 단계; 및
상기 제1연료조성물과 제2연료조성물을 혼합한 혼합물을 성형하는 단계;를 포함하는 폐기물을 이용한 고형연료의 제조방법.
Preparing a first fuel composition having at least one selected from the group consisting of waste wood pulp, sawdust, wood chip (WCF) pure wood pulp and wood;
Preparing a second fuel composition selected from one or more of crushed and pulverized mixed waste vinyl or dry crushed sewage and manure sludge; And
And molding the mixture of the first fuel composition and the second fuel composition.
상기 제1연료조성물과 제2연료조성물을 혼합하는 것은,
상기 제1연료조성물 15~99중량%와 제2연료조성물 1~85중량%를 혼합하는 것을 특징으로 하는 폐기물을 이용한 고형연료의 제조방법.
5. The method of claim 4,
Mixing the first fuel composition and the second fuel composition,
Wherein 15 to 99% by weight of the first fuel composition and 1 to 85% by weight of the second fuel composition are mixed.
상기 제2연료조성물을 준비하는 단계는,
상기 복합폐비닐을 파쇄한 후 자력 선별기로 금속성분을 1차 제거하는 단계;
상기 금속성분을 1차 제거한 복합폐비닐을 풍력 선별기를 통해 비중이 0.1이하인 것만을 선별하는 단계; 및
상기 선별한 복합폐비닐을 분쇄한 후 자력 선별기로 금속성분을 2차 제거하는 단계;를 포함하는 것을 특징으로 하는 폐기물을 이용한 고형연료의 제조방법.
5. The method of claim 4,
Wherein preparing the second fuel composition comprises:
Disrupting the composite waste vinyl, and removing the metal component by a magnetic separator;
Selectively collecting only the composite waste vinyl polymer having the specific gravity of 0.1 or less through the wind separator; And
And secondly removing metal components by a magnetic separator after crushing the selected composite waste vinyl.
상기 제1연료조성물 15~99중량%와 제2연료조성물 1~85중량%가 혼합되어 이루어진 것을 특징으로 하는 폐기물을 이용한 고형연료.
A process for producing a polyurethane foam, which is produced by the production method of any one of claims 4 to 6,
Wherein the solid fuel comprises 15 to 99% by weight of the first fuel composition and 1 to 85% by weight of the second fuel composition.
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