KR20030025985A - The preparation method of the solid fuel using the waste - Google Patents

The preparation method of the solid fuel using the waste Download PDF

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Publication number
KR20030025985A
KR20030025985A KR1020010058938A KR20010058938A KR20030025985A KR 20030025985 A KR20030025985 A KR 20030025985A KR 1020010058938 A KR1020010058938 A KR 1020010058938A KR 20010058938 A KR20010058938 A KR 20010058938A KR 20030025985 A KR20030025985 A KR 20030025985A
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South Korea
Prior art keywords
waste
solid waste
drying
solid fuel
fractions
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KR1020010058938A
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Korean (ko)
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이상열
이승균
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이상열
이승균
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Publication of KR20030025985A publication Critical patent/KR20030025985A/en

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/46Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/34Other details of the shaped fuels, e.g. briquettes
    • C10L5/36Shape
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/403Solid fuels essentially based on materials of non-mineral origin on paper and paper waste
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/406Solid fuels essentially based on materials of non-mineral origin on plastic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • C10L5/442Wood or forestry waste
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

PURPOSE: Provided is a method for preparing solid fuel using solid waste for solving a problem of lack of solid fuel, preventing soil and water contamination/pollution and reducing the solid waste. CONSTITUTION: The method comprises the steps of primarily crushing solid waste into fractions having a grain size of 4 to 7 cm and drying the solid waste fractions to have moisture content below 20 %; sorting non-combustible material from the solid waste fractions; secondarily crushing the solid waste fractions to have a grain size of 2 to 3 mm; feeding slaked lime to the secondarily crushed solid waste fractions to neutralizing the solid waste fractions; molding the neutralized solid waste fractions using a mold and extrusion cutting the molded neutralized solid waste fractions to have an adequate size, followed by drying/packing.

Description

폐기물을 이용한 고체연료 제조방법{The preparation method of the solid fuel using the waste}The preparation method of the solid fuel using the waste}

본 발명은 폐기물을 이용한 고체연료 제조방법에 관한 것으로서, 더욱 상세하게는 가연성폐기물을 이용하여 고체연료를 제조함으로서, 날로 심각해져 가는 고체연료 부족현상을 해소할 수 있고, 쓰레기처리문제를 해소할 수 있음은 물론, 토양오염 및 수질오염을 동시에 해소할 수 있도록 한 폐기물을 이용한 고체연료 제조방법에 관한 것이다.The present invention relates to a method for producing solid fuel using waste, and more particularly, by manufacturing solid fuel using flammable waste, it is possible to solve the growing shortage of solid fuel and solve waste disposal problems. Of course, the present invention relates to a method for producing solid fuel using wastes capable of simultaneously eliminating soil and water pollution.

산업사회의 발전 및 가정문화의 향상과 더불어 각종 쓰레기(이하"폐기물"이라 함)의 발생 량은 날로 증가하고 있고, 그 증가하는 쓰레기를 처리하기 위한 대처방안이 다양하게 연구되고 있으나, 현재에는 특별한 대안이 없어 해양투기 또는 매립하거나 소각처리 등의 방법으로 처리함에 따라서 해양오염과 매립으로 인한 땅 속의 산소결핍 현상이 발생되어 땅이 황폐화되고 소각으로 인한 연료낭비와 대기오염 및 수질오염이 발생되며, 사람들에게는 원인 모르는 피부질환과 호흡기계통의병이 발생되고 있는 현실이다.With the development of industrial society and the improvement of family culture, the generation of various wastes (hereinafter referred to as "waste") is increasing day by day, and various measures to deal with the increasing waste are being studied. As there is no alternative, disposal by ocean dumping, landfilling, or incineration treatment results in oxygen deficiency in the ground due to marine pollution and landfilling, resulting in desolation of the land, fuel waste, air pollution, and water pollution due to incineration. People are not aware of the cause of skin diseases and respiratory pain is occurring.

또한, 최근에는 환경문제가 어느 일 개국의 문제가 아닌 세계적인 관심사로 지구 환경문제가 심각하게 대두되어 세계 무역기구가 제창하는 공해산업의 수출금지 조치와 함께, 부족해 가는 연료의 무기화로 산유국의 발언권이 강화되고 있으며, 산업용 연료로 사용되는 자원의 양이 한정되어 몇 십년 후에는 고갈될 위기에 처해 있어 대체연료 개발이 시급한 실정이다.In addition, in recent years, environmental issues are not the issue of any one country, but global environmental issues are seriously raised, and the World Trade Organization's measures to prohibit the export of high-pollution industries and the weakening of the weapons of oil producers have the right to speak. As it is being strengthened and the amount of resources used for industrial fuel is limited, it is in danger of being depleted after several decades. Therefore, it is urgent to develop alternative fuel.

따라서, 종래에는 상기의 시급한 대체연료 문제를 해소하기 위한 방편으로 동물체의 배설물과 각종 쓰레기 및 폐유 등을 일정 배합비 및 일정조건에서 혼합 발효시킨 후, 폐지와 혼합하면서 일정량을 성형하는 연료제조방법이 특허출원 제1997-3375호에 제시되어 있다.Therefore, in the related art, as a way to solve the urgent alternative fuel problem, a fuel manufacturing method for mixing and fermenting animal wastes and various wastes and waste oils at a predetermined compounding ratio and under certain conditions, and then mixing them with waste paper is patented. It is presented in application 1997-3375.

상기 특허출원 제 1997-3375호의 연료제조방법을 살펴보면, 준비된 동물체의 배설물과 쓰레기는 약 1:2의 비율로 용기에 넣고, 약 15일이상 발효시킨 다음 준비된 폐지를 넣어 혼합시킨 후, 일정량의 폐유를 투입하여 혼합하고, 일정규격으로 포장하는 것으로서, 이의 구체적인 방법을 살펴보면 다음과 같다.Looking at the fuel manufacturing method of the patent application No. 1997-3375, the excrement and waste of the prepared animal body is put in a container at a ratio of about 1: 2, fermented for about 15 days or more, mixed with the prepared waste paper, and then a predetermined amount of waste oil Into the mixing, and packaging to a certain standard, look at the specific method thereof as follows.

먼저 준비된 동물체의 배설물과 일반 가정 및 산업체에서 발생된 금속물질이 제거된 쓰레기를 1:2로 혼합하여 15일 이상 자연 발효시킨 다음, 이에 폐지를 넣고 혼합하여 2차 발효한다.First, the excreted animal body and the waste from which metals generated in general households and industries are removed 1: 2 are mixed and fermented naturally for 15 days or more, and then, the waste paper is mixed and mixed for the second fermentation.

이때 동물체의 배설물과 쓰레기 및 폐지의 배합비는 2:4:4 정도이다. 그리고 상기 2차 발효된 발효물에 폐유를 넣고 충분히 혼합하여 상기 폐유가 발효물에 쓰며들게 함으로서 연료의 제조방법이 완료되는 것이다.At this time, the mixing ratio of animal waste and waste and waste paper is about 2: 4: 4. Then, the waste oil is added to the fermented fermented secondary, and the mixture is sufficiently mixed so that the waste oil is used in the fermented product.

그러나, 상기의 연료제조방법은 제조공정상의 간단함은 있으나, 폐유 사용으로 인한 연소시 인체에 유해한 독가스가 발생하여 대기오염을 가중시키는 문제점이 있어, 상기 연료를 사용하기 위해서는 별도의 폐 가스 처리장치를 설치해야함으로 그에 따른 경제성이 떨어지는 문제점이 있었다.However, the above fuel manufacturing method is simple in the manufacturing process, but there is a problem in that poisonous gas harmful to the human body is generated during combustion due to the use of waste oil, thereby increasing the air pollution. In order to use the fuel, a separate waste gas treatment apparatus is used. There was a problem that the economical fall according to the installation.

또 다른 상태의 종래 고체연료 제조방법은 가정, 식품제조업체, 제철소, 폐차장, 제지업체, 하수처리장, 축산폐기물, 섬유업체, 방적공장, 등에서 발생되는 각종 폐기물을 가공 처리하고, 이를 고형화시켜 연료로 재활용 할 수 있는 기술이 특허출원 제1996-018136호에 제시되어 있다.The conventional solid fuel production method in another state processes various wastes generated from households, food manufacturers, steel mills, junkyards, paper companies, sewage treatment plants, livestock waste, textile companies, spinning plants, etc., and solidifies them to be recycled as fuel. A technique that can be done is shown in patent application No. 1996-018136.

상기 특허출원 제1996-018136호의 연료제조방법을 살펴보면, 산업현장에서 발생되는 폐 엔진오일, 폐 기계오일, 산업현장의 폐수 등의 광물유를 용적 5㎥의 가열용기 내에 약 2ton 정도 투입하여 120℃전후까지 간접 가열시킨 후, 수분 85%정도 포함되어 있는 폐기물 2.5ton정도를 가열용기 내에 투입하여 교반 가열한 다음, 초기에 20분 정도를 저 진공상태로 탈수하면서 점차 연속적으로 가열용기 내를 500∼750㎜/Hg의 진공상태로 하고, 기름의 온도를 90℃∼100℃정도 유지하면, 폐기물의 수분함량이 5%정도로 탈수되면서 고형연료를 얻게 되는 것이다.Looking at the fuel manufacturing method of the patent application No. 1996-018136, the mineral oil, such as waste engine oil, waste machine oil, industrial waste water generated in the industrial site is put into about 2 tons in a heating vessel with a volume of 5 ㎥ around 120 ℃ After indirect heating up to about 2.5 tons of waste containing about 85% of water in a heating vessel and stirred and heated, and then gradually dehydrated for about 20 minutes in a low vacuum state gradually 500 ~ 750 inside the heating vessel If the temperature of the oil is maintained at 90 ° C. to 100 ° C. in a vacuum of mm / Hg, the waste water is dehydrated at about 5% to obtain solid fuel.

이상의 방법으로 제조되는 상기 연료제조방법은 전술한 특허출원 제1997-3375호와 마찬가지로 폐유를 사용하기 때문에 연료가 연소되면서 인체에 유해한 독가스가 배출되어 대기오염을 가중시키는 문제점이 있고, 또 제조상의 어려움이 있으며, 제조과정이 복잡하여 경제성이 상실되는 문제점이 지적되고 있었다.Since the fuel manufacturing method manufactured by the above method uses waste oil as in the aforementioned Patent Application No. 1997-3375, there is a problem in that poisonous gases are harmful to the human body as fuel is burned, thereby increasing air pollution, and manufacturing difficulties. There is a problem that the manufacturing process is complicated and the economics are lost.

본 발명은 상기와 같은 제반 문제점을 감안하여 이를 해소하고자 발명한 것으로서, 그 목적은 가연성폐기물을 수거하여 분쇄 및 건조하고, 그중 비가연성물질을 선별해 낸 다음, 다시 이를 성형할 수 있는 크기로 분쇄하여 이에 중화제 및 점결제 역할을 소석회를 투입한 다음, 성형기를 이용하여 원하는 형상으로 성형하고, 최종 건조함으로서 발열량이 높은 고체연료를 제조함은 물론, 폐기물을 재활용하여 작금에 문제시되고 있는 폐 쓰레기 처리문제를 해소하고, 연소시 발생하는 대기오염물질 발생을 최소화할 수 있도록 한 폐기물을 이용한 고체연료 제조방법을 제공함에 있다.The present invention has been invented to solve the above problems in consideration of the above problems, the object is to collect and combust the combustible waste, and to dry, select the non-flammable material from among them, and then to crush the size to form again Therefore, by adding slaked lime as a neutralizer and caking agent, it is molded into a desired shape by using a molding machine, and finally dried to produce a solid fuel having a high calorific value, as well as recycling waste to dispose of the waste, which is currently a problem. It is to provide a solid fuel manufacturing method using waste to solve the problem and to minimize the generation of air pollutants generated during combustion.

상기 목적을 달성하기 위한 본 발명의 폐기물을 이용한 고체연료 제조방법에 대한 특징적인 기술적 구성을 설명하면 다음과 같다.Referring to the technical features of the solid fuel production method using the waste of the present invention for achieving the above object.

본 발명의 폐기물을 이용한 고체연료 제조방법은 수거된 폐기물을 입자크기 4∼7cm로 1차 분쇄하고, dl를 수분함량 20% 이하가 되게 건조하는 단계; 상기 1차 건조된 폐기물 중 비가연성 물질을 선별해 내고, 이를 입자크기 2∼3mm로 2차 분쇄하는 단계; 상기 2차 분쇄된 폐기물에 소석회를 투입하고, 혼합하여 상기 폐기물을 중화처리 하는 단계; 상기 중화처리 된 폐기물을 성형기에 투입하여 성형하고, 이를 원하는 크기로 절단하는 단계; 상기 절단된 성형품을 최종건조 처리하고, 이를 포장하는 단계로 이루어진다.Solid fuel production method using the waste of the present invention comprises the steps of first grinding the collected waste to a particle size of 4 ~ 7cm, and drying the dl to 20% or less moisture content; Screening the non-combustible material from the first dried waste and crushing it to a particle size of 2 to 3 mm; Injecting slaked lime into the second crushed waste and mixing the same to neutralize the waste; Injecting the neutralized waste into a molding machine and shaping the waste to a desired size; The cut molded article is subjected to a final drying process and packaging.

그리고, 상기 폐기물은 가연성 음식쓰레기, 폐지, 합성수지, 가연성 일반쓰레기, 폐목재 중 어느 하나 또는 2가지 이상이 혼합된 것이고, 상기 성형기에서 성형되는 성형품의 형태는 파이프형태이며, 상기 폐기물 및 성형품의 건조는 건조로에서 이루어지고 그 건조온도는 90∼120℃이다.The waste is any one or two or more of flammable food waste, waste paper, synthetic resin, combustible general waste, and waste wood, and the shape of the molded product formed in the molding machine is in the form of a pipe, and the waste and the molded article are dried. Is made in a drying furnace and its drying temperature is 90-120 ° C.

이와 같은 특징을 갖는 본 발명의 폐기물을 이용한 고체연료 제조방법을 각 단계별로 설명하면 다음과 같다.Referring to each step of the solid fuel manufacturing method using the waste of the present invention having such characteristics as follows.

(제1단계)(Step 1)

본 발명의 제1단계는 폐기물을 수거하고 그 수거된 폐기물을 분쇄한 후 건조하는 단계로서, 먼저 폐기물(음식물쓰레기, 폐 합성수지, 폐지, 폐 목재, 일반쓰레기, 폐 고무, 폐 섬유, 폐 가죽, 농산물쓰레기, 기타 가연성쓰레기)을 수거하여 비가연성물질을 선별해 낸 후, 그 선별된 비가연성물질은 별도로 처리하고, 가연성물질은 분쇄기에 투입하여 4∼7cm로 크기로 1차 분쇄한 후, 이를 건조로에 투입하여 90∼120℃의 온도로 수분함량 20% 이하가 되게 건조한다.The first step of the present invention is a step of collecting waste and pulverizing the collected waste and then drying, firstly waste (food waste, waste synthetic resin, waste paper, waste wood, general waste, waste rubber, waste fiber, waste leather, After collecting non-combustibles by collecting agricultural wastes and other combustible wastes, the selected non-combustibles are treated separately, and combustibles are put into a grinder and crushed first to a size of 4-7 cm. It is added to a drying furnace and dried to a water content of 20% or less at a temperature of 90 to 120 ° C.

상기 가연성물질을 분쇄기를 이용하여 4∼7cm로 크기로 분쇄하는 이유는 그 이하가 되면 입자상호간에 뭉쳐져서 건조속도가 느려지고 목적하는 수분함량이 20%이하를 유지할 수 없으며, 그 이상이 되면 입장상호간에 뭉치는 문제점은 해소할 수 있으나, 이 역시 건조속도가 느려지고 목적하는 수분함량이 20%이하를 유지할 수 없는 문제점이 있다.The reason for pulverizing the combustible material into the size of 4-7 cm by using a crusher is that when it is less than it, the particles are aggregated between the particles, and the drying speed is slowed, and the desired moisture content cannot be maintained below 20%. The problem can be solved in the bundle, but this also has a problem that the drying speed is slow and the desired moisture content can not be maintained below 20%.

따라서, 제1단계에서의 분쇄기에서 분쇄되는 입자크기는 4∼7cm를 유지함이 바람직하다.Therefore, the particle size to be crushed in the mill in the first step is preferably maintained 4 ~ 7cm.

또, 상기 4∼7cm 크기로 분쇄된 가연성폐기물을 건조로에 투입하여 90∼120℃로 건조하는데, 그 건조방법은 건조로에 열풍을 불어넣어 건조로내부의 분위기 온도를 90∼120℃로 유지하여 건조한다.In addition, the combustible waste pulverized to 4-7cm size is put into a drying furnace and dried at 90-120 ° C. The drying method blows hot air into the drying furnace to dry it while maintaining the ambient temperature inside the drying furnace at 90-120 ° C. .

단, 상기 건조온도가 90℃이하이면 정해진 시간내에 수분함량 20%이하가 되게 건조할 수 없고, 120℃이상이 되면 가연성폐기물이 타버릴 염려가 있다.However, if the drying temperature is less than 90 ℃ can not be dried to less than 20% of the moisture content within a predetermined time, if there is more than 120 ℃ there is a risk of burning the flammable waste.

따라서, 건조온도는 90∼120℃를 유지하는 것이 바람직하다.Therefore, it is preferable to maintain a drying temperature of 90-120 degreeC.

또한, 상기 건조로에서 건조되는 가연성 폐기물은 교반을 하면서 건조하는 것이 바람직하고, 수분함량이 20% 이상이면 하기에서 설명되는 각 단계들의 작업이 원활하게 이루어지지 못하는 문제점이 발생한다.In addition, the combustible waste to be dried in the drying furnace is preferably dried while stirring, there is a problem that the operation of each step described below is not smoothly performed if the moisture content is 20% or more.

(제2단계)(Step 2)

본 발명의 제2단계는 상기 제1단계의 과정이 끝난 가연성폐기물에 함유된 비가연성물질을 선별해 내고, 그 비가연성물질이 선별된 가연성폐기물을 다시 분쇄기에 투입하여 입자크기 2∼3mm로 분쇄하는 단계인데, 상기 비가연성물질을 선별하는 이유는 비가연성물질이 선별되지 않게 되면 하기에서 설명되는 성형작업시 그 성형이 원활하게 이루어지지 않는 문제점이 발생함은 물론, 고체연료를 완성했을 발열량이 떨어지는 문제점이 발생한다.In the second step of the present invention, the non-combustible material contained in the combustible wastes of which the process of the first step is completed is sorted out, and the combustible wastes from which the non-combustible material is selected are put back into the grinder and pulverized to a particle size of 2 to 3 mm. The reason for selecting the non-combustible material is that when the non-combustible material is not selected, a problem occurs that the molding is not smoothly performed during the molding operation described below, and the calorific value of the solid fuel is completed. Falling problem occurs.

또 상기 비가연성물질이 선별된 가연성폐기물을 분쇄기에 투입하여 2∼3mm 크기로 분쇄하는 이유는 그 이상이 되면 성형이 정상적으로 이루어지지 않고, 그 이하가 되면 성형성은 좋으나, 하기에서 설명되는 중화제를 투입한 후, 혼합할 때에 원활한 혼합이 이루어지지 않는 문제점이 있다.In addition, the reason why the non-combustible material is combustible waste sorted into a crusher and crushed to a size of 2 to 3 mm is not formed if it is more than that, and if it is less than that, the moldability is good, but the neutralizing agent described below is added. After that, there is a problem in that smooth mixing is not performed when mixing.

(제3단계)(Step 3)

본 발명의 제3단계는 상기 제2단계의 과정이 끝난 가연성물질을 혼합기에 투입하고, 이에 중화제이며 점결제 역할을 하는 소석회를 투입하여 혼합하는 단계로서, 상기 소석회를 투입하는 이유는 산성인 가연성폐기물을 중성으로 바꾸기 위함이다.The third step of the present invention is a step of adding the combustible material of the second step of the process to the mixer, and adding and mixing the slaked lime which acts as a neutralizer and a caking agent, and the reason for adding the slaked lime is acidic combustible To convert the waste to neutral.

상기 제조 완료된 고체연료가 산성이면, 연소시 인체에 유해한 물질이 가스화 되어 방출됨으로 이는 대기오염은 물론, 건강을 해치는 원인이 된다.If the produced solid fuel is acidic, the harmful substances to the body during the combustion is released by gasification, which causes air pollution, as well as damage to health.

또, 상기 소석회는 점결성을 가지고 있기 때문에 본 발명에서 목적하는 고체의 형상을 유지할 수 있고, 그리고 상기 소석회는 경화제 역할을 동시에 하기 때문에 소정의 강도를 유지하게 된다.In addition, since the slaked lime has a caking property, it is possible to maintain the shape of the solid desired in the present invention, and the slaked lime maintains a predetermined strength because it simultaneously acts as a curing agent.

(제4단계)(Step 4)

본 발명의 제4단계는 상기 제3단계의 과정이 끝난 가연성물질을 성형기에 투입하여 소정의 원하고자 하는 형상으로 성형하고, 이를 원하는 크기로 절단하는 단계로서, 본 발명에서 사용하는 성형기는 가연성물질을 압출하여 뽑아내는 것으로서, 그 압출공의 형상이 파이프형태로 압출되게 되어 있어 상기 가연성물질의 파이프형태로 게속 압출된다.The fourth step of the present invention is a step of inserting the combustible material of the third step is completed in a molding machine to a predetermined desired shape, and cutting it to a desired size, the molding machine used in the present invention is a combustible material By extruding, the shape of the extruded hole is extruded in the form of a pipe, and continuously extruded in the form of a pipe of the combustible material.

그리고, 상기 파이프형태로 압출되는 성형품은 소비자가 원하는 크기로 절단한다.The molded article extruded in the form of a pipe is cut to a size desired by the consumer.

(제5단계)(Step 5)

본 발명의 제5단계는 상기 제4단계의 과정이 끝난 성형품을 건조로에 투입하여 90∼120℃로 건조하고, 이를 포장하는 단계로서, 건조하는 방법은 건조로에 열풍을 불어넣어 건조로 내부의 분위기 온도를 90∼120℃로 유지하여 건조한다.The fifth step of the present invention is a step of putting the molded article of the fourth step is completed in a drying furnace to dry at 90 ~ 120 ℃, and packing it, the drying method is to blow the hot air into the drying furnace to dry the atmosphere inside the drying furnace The temperature is kept at 90 to 120 ° C. and dried.

단, 상기 건조온도가 90℃이하이면 정해진 시간내에 수분함량 10%이하가 되게 건조할 수 없고, 120℃이상이 되면 가연성폐기물이 타버릴 염려가 있다.However, if the drying temperature is less than 90 ℃ can not be dried to less than 10% of the moisture content within a predetermined time, if the temperature is more than 120 ℃ may burn the flammable waste.

따라서, 건조온도는 90∼120℃를 유지하는 것이 바람직하다.Therefore, it is preferable to maintain a drying temperature of 90-120 degreeC.

한편, 수분함량이 10% 이상이면 발화시 원활하게 발화되지 못하는 문제점이 발생한다.On the other hand, if the moisture content is more than 10% there is a problem that does not ignite smoothly when ignited.

따라서, 제조 완료된 고체연료는 수분함량이 10%이하여야 한다. 또, 상기 제4단계에서 본 발명의 고체연료 형태를 파이프형태로 한 것은 발열량을 높이기 위함이다.Therefore, the manufactured solid fuel should have a water content of 10% or less. In addition, the solid fuel form of the present invention in the fourth step in the form of a pipe is to increase the amount of heat generated.

이하 본 발명의 실시 예를 들어 설명하면 다음과 같다.Hereinafter, an embodiment of the present invention will be described.

[실시예1]Example 1

본 발명의 실시 예1은 가연성폐기물(목재, 폐지 합성수지, 고무)을 수거하여, 이를 7cm이하 크기로 1차 분쇄하고, 수분함량 20%정도가 되게 건조한 다음, 그중 비가연성 물질인 금속제 등을 선별해 내고, 다시 3mm정도 크기로 분쇄하여 소석회와 함께 혼합기에 투입하여 혼합한 후, 성형기에 투입하여 파이프형태로 압출한 다음, 길이 10cm 크기로 절단하고 수분함량 3%이하가 되게 최종 건조하였다.In Example 1 of the present invention, the combustible waste (wood, waste paper synthetic resin, rubber) is collected, firstly crushed to 7 cm or less in size, dried to a moisture content of about 20%, and then selected from non-combustible metals, etc. After crushing, the mixture was crushed to about 3 mm in size, mixed with hydrated lime and mixed in the mixer, and then fed into a molding machine, extruded into a pipe shape, cut into 10 cm in length, and finally dried to have a water content of 3% or less.

이와 같이하여 제조된 파이프형태의 연료를 연소로에 투입하고, 발열량을 측정해본 결과, 그 발열량은 6000kcal가 나왔다.The pipe-type fuel thus produced was introduced into the combustion furnace, and the calorific value was measured. As a result, the calorific value was 6000 kcal.

그리고, 상기 방법으로 제조된 고체연료에서는 대기오염의 주범이며, 인체에유해한 다이옥신은 거의 발생하지 않았고, 기타 중금속은 0.01ng/Nm2이하가 발생하였다.In addition, in the solid fuel produced by the above method, the main culprit of air pollution, dioxin harmful to the human body was hardly generated, and other heavy metals were less than 0.01 ng / Nm 2 .

[실시예2]Example 2

본 발명의 실시예 2는 가연성폐기물(합성수지, 섬유, 가죽, 농산물쓰레기)을 수거하여, 이를 5cm이하 크기로 1차 분쇄하고 수분함량 15%정도가 되게 건조한 다음, 그중 비가연성 물질인 금속제 등을 선별해 내고, 다시 2mm정도 크기로 분쇄하여 소석회와 함께 혼합기에 투입하여 혼합한 후, 성형기에 투입하여 파이프형태로 압출한 다음, 길이 5cm 크기로 절단하고, 수분함량 3%가 되게 최종 건조하였다.In Example 2 of the present invention, the combustible waste (synthetic resin, fiber, leather, agricultural waste) is collected, firstly crushed to a size of 5 cm or less, dried to 15% moisture content, and then made of non-combustible metals, etc. After sorting and crushing again to about 2mm in size and mixed with calcined lime in a mixer, and then put into a molding machine, extruded in the form of a pipe, cut into a size of 5cm in length, and finally dried to 3% moisture content.

이와 같이하여 제조된 파이프형태의 연료를 연소로에 투입하고, 발열량을 측정해 본 결과, 그 발열량은 5500kcal가 나왔다.The pipe-type fuel thus produced was introduced into the combustion furnace, and the calorific value was measured. As a result, the calorific value was 5500 kcal.

그리고, 상기 방법으로 제조된 고체연료에서는 대기오염의 주범이며, 인체에 유해한 다이옥신 및 중금속의 발생은 상기 실시 예1과 거의 유사하였다.In addition, in the solid fuel produced by the above method, the main culprit of air pollution, and the generation of dioxins and heavy metals harmful to the human body were almost similar to those of Example 1.

[실시예3]Example 3

본 발명의 실시 예3은 가연성폐기물(음식물쓰레기, 일반쓰레기, 섬유, 가죽,)을 수거하여, 이를 10cm이하 크기로 1차 분쇄하고, 수분함량 20%정도가 되게 건조한 다음, 그중 비가연성 물질인 금속제 등을 선별해 내고, 다시 3mm정도 크기로 분쇄하여 소석회와 함께 혼합기에 투입하여 혼합한 후, 성형기에 투입하여 파이프형태로 압출한 다음, 길이 5cm정도 크기로 절단하고, 수분함량 5%이하가 되게 최종 건조하였다.Example 3 of the present invention collects combustible waste (food waste, general waste, fiber, leather,), and firstly crushed it to a size of 10 cm or less, and dried to 20% moisture content, among which is a non-combustible material The metal is sorted out, crushed into 3mm size, put into the mixer with slaked lime, mixed into the mixer, and then put into a molding machine, extruded into a pipe shape, cut into 5cm lengths, and less than 5% of water content. Final drying.

이와 같이하여 제조된 파이프형태의 연료를 연소로에 투입하고 발열량을 측정해본 결과, 그 발열량은 상기 실시 예1 및 실시 예2보다 약간적은 4500kcal가 나왔다.As a result of injecting the pipe-type fuel thus prepared into the combustion furnace and measuring the calorific value, the calorific value was 4500 kcal which was slightly smaller than those of the first and second embodiments.

그리고, 상기 방법으로 제조된 고체연료에서는 대기오염의 주범이며, 인체에 유해한 다이옥신 및 중금속의 발생은 0.017ng/Nm2이 발생하였다.In addition, in the solid fuel produced by the above method, the main culprit of air pollution, the generation of dioxins and heavy metals harmful to humans occurred 0.017ng / Nm 2 .

이상과 같은 방법으로 제조된 본 발명의 고체연료는 규격화하여 성형할 수 있으므로 보관 및 운반이 용이하고 포장이 쉬우며, 발열량이 높아 각종발전소 및 보일러의 연료로 사용할 수 있는 장점이 있다.Since the solid fuel of the present invention manufactured by the above method can be molded by standardization, it is easy to store and transport, easy to package, and has a high calorific value, which can be used as fuel for various power plants and boilers.

이상과 같은 본 발명은 폐기물을 재활용함으로서 경제적 가치가 높고, 폐기물을 매립하고자 하는 부지확보가 필요 없으며, 환경보존의 효과가 있음은 물론, 날로 심각해져 가는 고체연료 부족현상을 해소할 수 있고, 쓰레기처리문제를 해소할 수 있으므로, 토양오염 및 수질오염을 동시에 해소할 수 있는 특유의 효과가 있다.The present invention as described above has a high economic value by recycling waste, there is no need to secure the site to bury the waste, there is an effect of environmental preservation, as well as can solve the serious shortage of solid fuel, and waste disposal Since the problem can be solved, there is a peculiar effect that can simultaneously solve soil pollution and water pollution.

Claims (4)

수거된 폐기물을 입자크기 4∼7cm로 1차 분쇄하고, 이를 수분함량 20% 이하가 되게 건조하는 단계;Firstly crushing the collected waste to a particle size of 4 to 7 cm and drying it to a water content of 20% or less; 상기 1차 건조된 폐기물 중 비가연성 물질을 선별해 내고, 이를 입자크기 2∼3mm로 2차 분쇄하는 단계;Screening the non-combustible material from the first dried waste and crushing it to a particle size of 2 to 3 mm; 상기 2차 분쇄된 폐기물에 소석회를 투입하고, 혼합하여 상기 폐기물을 중화처리 하는 단계;Injecting slaked lime into the second crushed waste and mixing the same to neutralize the waste; 상기 중화처리 된 폐기물을 성형기에 투입하여 성형하고, 이를 원하는 크기로 절단하는 단계;Injecting the neutralized waste into a molding machine and shaping the waste to a desired size; 상기 절단된 성형품을 최종건조 처리하고, 이를 포장하는 단계를 포함하는 폐기물을 이용한 고체연료 제조방법.Final dry treatment of the cut molded article, and packaging the solid fuel production method comprising the step of packaging the same. 제1항에 있어서, 상기 폐기물은 가연성 음식쓰레기, 폐지, 합성수지, 가연성 일반쓰레기, 폐목재 중 어느 하나 또는 2가지 이상이 혼합된 것임을 특징으로 하는 폐기물을 이용한 고체연료 제조방법.The method of claim 1, wherein the waste is one or two or more of flammable food waste, waste paper, synthetic resin, combustible general waste, and waste wood. 제1항에 있어서, 상기 성형기에서 성형되는 성형품의 형태는 파이프형태임을특징으로 하는 폐기물을 이용한 고체연료 제조방법.The method of manufacturing a solid fuel using waste according to claim 1, wherein the molded article formed in the molding machine is in the form of a pipe. 제1항에 있어서, 상기 폐기물 및 성형품의 건조는 건조로에서 이루어지고 그 건조온도는 90∼120℃임을 특징으로 하는 폐기물을 이용한 고체연료 제조방법.The method of claim 1, wherein the drying of the waste and the molded article is made in a drying furnace and the drying temperature is 90 ~ 120 ℃.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030091597A (en) * 2002-05-28 2003-12-03 엽정화 The method manufacture and solidity coal use wood
KR100443899B1 (en) * 2001-10-18 2004-08-09 장영광 Manufacturing method of solid fuel using food waste
KR100449517B1 (en) * 2002-04-10 2004-09-18 배상윤 Method for manufacturing refuse derived fuel in soild state which comprises food waste containing grain and vegetable, general waste containing paper and plastic, and coals
KR100932561B1 (en) * 2007-12-13 2009-12-17 양송철 Osteoblasting apparatus and method
KR101007651B1 (en) * 2010-03-31 2011-01-13 산림조합중앙회 The fuel pellet which uses the lignum materials and the lumber and the manufacturing method
KR101347777B1 (en) * 2010-12-10 2014-01-03 주식회사 중앙 Method for preparing solid fuel using combustible waste

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR920000908A (en) * 1990-06-12 1992-01-29 김태엽 Manufacturing method of waste derived fuel
KR930019806A (en) * 1992-03-25 1993-10-19 전병연 Waste-themed Solid Fuel Manufacturing System
JPH06108075A (en) * 1992-09-25 1994-04-19 Mitsubishi Heavy Ind Ltd Production 0f solid fuel from waste material
JPH08311465A (en) * 1995-05-22 1996-11-26 Ishikawajima Harima Heavy Ind Co Ltd Production of solid refuse fuel
KR100202462B1 (en) * 1997-07-08 1999-06-15 서상기 Apparatus for converting household and/or other waste to solid fuel
KR20020059074A (en) * 2000-12-30 2002-07-12 이 상 종 Packet was lost

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR920000908A (en) * 1990-06-12 1992-01-29 김태엽 Manufacturing method of waste derived fuel
KR930019806A (en) * 1992-03-25 1993-10-19 전병연 Waste-themed Solid Fuel Manufacturing System
JPH06108075A (en) * 1992-09-25 1994-04-19 Mitsubishi Heavy Ind Ltd Production 0f solid fuel from waste material
JPH08311465A (en) * 1995-05-22 1996-11-26 Ishikawajima Harima Heavy Ind Co Ltd Production of solid refuse fuel
KR100202462B1 (en) * 1997-07-08 1999-06-15 서상기 Apparatus for converting household and/or other waste to solid fuel
KR20020059074A (en) * 2000-12-30 2002-07-12 이 상 종 Packet was lost

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100443899B1 (en) * 2001-10-18 2004-08-09 장영광 Manufacturing method of solid fuel using food waste
KR100449517B1 (en) * 2002-04-10 2004-09-18 배상윤 Method for manufacturing refuse derived fuel in soild state which comprises food waste containing grain and vegetable, general waste containing paper and plastic, and coals
KR20030091597A (en) * 2002-05-28 2003-12-03 엽정화 The method manufacture and solidity coal use wood
KR100932561B1 (en) * 2007-12-13 2009-12-17 양송철 Osteoblasting apparatus and method
KR101007651B1 (en) * 2010-03-31 2011-01-13 산림조합중앙회 The fuel pellet which uses the lignum materials and the lumber and the manufacturing method
KR101347777B1 (en) * 2010-12-10 2014-01-03 주식회사 중앙 Method for preparing solid fuel using combustible waste

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