KR20010067490A - Sold fuel manufacturing method use waste plastic and the waste plastic thereof - Google Patents

Sold fuel manufacturing method use waste plastic and the waste plastic thereof Download PDF

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KR20010067490A
KR20010067490A KR1020010002192A KR20010002192A KR20010067490A KR 20010067490 A KR20010067490 A KR 20010067490A KR 1020010002192 A KR1020010002192 A KR 1020010002192A KR 20010002192 A KR20010002192 A KR 20010002192A KR 20010067490 A KR20010067490 A KR 20010067490A
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waste
synthetic resin
waste synthetic
solid fuel
calcium oxide
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KR1020010002192A
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Korean (ko)
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KR100405169B1 (en
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문규봉
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문규봉
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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
    • C10L5/406—Solid fuels essentially based on materials of non-mineral origin on plastic
    • 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
    • C10L2290/14—Injection, e.g. in a reactor or a fuel stream during fuel production
    • C10L2290/141—Injection, e.g. in a reactor or a fuel stream during fuel production of additive or catalyst
    • 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
    • C10L2290/32—Molding or moulds
    • 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

PURPOSE: Provided is a process for producing solid fuel by using a waste synthetic resin such as waste synthetic fiber, waste synthetic rubber, waste PE, waste PP, waste PS, waste paper, and etc, which has high heating value and is easy to store and treat. CONSTITUTION: The process comprises the steps of: filtering moisture from the waste synthetic resin and selecting non-flammable substances from the moisture filtered waste synthetic resin; grinding the selected waste synthetic resin; adding additives such as calcium oxide and synthetic zeolite to the ground waste synthetic resin, wherein the additives reduce hazardous ingredients such as NOx, SOx, dioxin, and hydrochloric oxides and eliminate heat-cracking; adding the mixture to a mold and heating to form and cutting.

Description

폐합성수지를 이용한 고체연료 제조방법 및 그 방법으로 제조된 고체연료{Sold fuel manufacturing method use waste plastic and the waste plastic thereof}Solid fuel manufacturing method using waste synthetic resin and solid fuel manufactured by the same method

본 발명은 폐합성수지를 이용한 고체연료 제조방법 및 그 방법으로 제조된 고체연료에 관한 것으로서, 더욱 상세하게는 산업발전의 고도화와 함께 점차 늘어나면서 사회문제화 되고 있는 산업폐기물이라 할 수 있는 폐합성수지 즉, 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS, 폐지 등을 이용하여 취급 및 보관이 용이하고 발열량이 높은 고체연료를 제조함으로서 에너지부족 현상을 해소할 수 있도록 한 것이다.The present invention relates to a method for producing a solid fuel using a waste synthetic resin and a solid fuel produced by the method, more specifically, a waste synthetic resin that can be referred to as industrial waste, which is gradually becoming a social problem with the advancement of industrial development. Using waste synthetic fiber, waste synthetic rubber, waste PE, waste PP, waste PS, waste paper, etc., it is easy to handle and store and manufacture solid fuel with high calorific value to solve the energy shortage phenomenon.

산업발전의 고도화 즉 전자, 전기, 통신의 발달과 그들 기기들의 사용이 급격히 증가하고 보편화됨에 따라 동(Cu)의 수요는 매년 증가하고 있으며, 그 동의 사용이 증가함에 따라 피복재로 사용되는 폐합성수지인 폐합성섬유, 폐합성고무, 폐지, 폐PE, 폐PP, 폐PS 등도 늘어나고 있는 추세이다.The demand for copper is increasing year by year due to the rapid development and generalization of industrial development, that is, the development of electronics, electricity, and communication, and the use of their devices, and as the use of copper increases, Waste synthetic fiber, waste synthetic rubber, waste paper, waste PE, waste PP and waste PS are also on the rise.

이와 같이 동의 사용이 증가함에 따라 늘어나고 있는 동의 피복재인 폐합성수지는 재활용가치가 충분히 있으며, 특히 상기 폐합성수지의 특성상 연료로서의 사용이 그 무엇보다 활용가치가 높다할 수 있다.As such, as the use of copper increases, waste synthetic resin, which is an increasing amount of copper cladding, has a sufficient recycling value, and in particular, the use of fuel as a fuel may have higher utilization value than that of the waste synthetic resin.

그러나 작금에는 상기 동을 피복하는 피복재로 사용되고 있는 폐합성수지 즉 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS, 폐지 등은 탈피시켜 버리고, 동 만을 회수하여 재활용하고 있는 실정이다.However, in recent years, waste synthetic resins used as a coating material for covering copper, that is, waste synthetic fibers, waste synthetic rubber, waste PE, waste PP, waste PS, waste paper, etc., have been removed, and only copper is recovered and recycled.

상기 버려지는 폐합성수지는 산업폐기물로 취급되어 막대한 비용을 투자해가며 소각 등을 방법으로 처리하고 있는 바, 상기 폐합성수지를 소각하게 되면 질산, 황산, 다이옥신, 산화물 등이 발생하여 대기오염은 물론 인체에 유해함을 주어 각종 질병을 유발시킨다.The discarded synthetic resin is treated as industrial waste, investing enormous costs, and incineration is processed by the method. When the waste synthetic resin is incinerated, nitric acid, sulfuric acid, dioxin, oxide, etc. are generated, and thus, air pollution as well as human body are caused. Harm to cause various diseases.

따라서 상기 동을 재활용하고자 탈피되는 폐합성수지인 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS 폐지 등의 재활용은 국가경제에도 지대한 영향을 줄 수 있음은 물론 상기 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS,폐지 등이 연료로서 재활용된다면 에너지부족 현상에도 일익을 담당할 수 있을 것이다.Therefore, the recycling of waste synthetic fiber, waste synthetic rubber, waste PE, waste PP, waste PS waste paper, etc., which are stripped to recycle the copper can have a great effect on the national economy as well as the waste synthetic fiber, waste synthesis If rubber, waste PE, waste PP, waste PS, waste paper, etc. are recycled as fuels, energy shortages can also play a role.

종래에도 가연성 쓰레기를 가압 성형하여 고체연료를 얻기 위한 가연성 쓰레기를 이용한 고체연료 성형방법이 제공된 바 있다.Conventionally, there has been provided a solid fuel molding method using a combustible waste for pressurizing the combustible waste to obtain a solid fuel.

이는 종이류, 섬유류 합성수지류 등의 쓰레기를 분쇄하고 그 분쇄된 쓰레기를 불규칙하게 섞어서 가압 이송하는 중에 조연제를 분사 혼합하며 이후 상기 쓰레기를 앞에서 가하여진 가압력에 의해 노즐을 통과하도록 함으로서 소정형상의 고체연료를 성형하도록 된 쓰레기를 이용한 고체연료 성형방법에 있어서,This grinds waste such as paper, fiber, synthetic resin, etc., and mixes the crushed waste irregularly and sprays and mixes the coarse agent during pressurized transportation, and then passes the waste through the nozzle by the pressing force applied in front of the solid fuel of a predetermined shape. In the solid fuel molding method using the waste to be molded,

상기 노즐을 통과하는 쓰레기에 비틀림을 부여하여 쓰레기의 각 구성물간의 결합구조를 복잡화함으로서 노즐을 통하여 얻어지는 고체연료의 부서짐 현상을 방지하도록 한 기술이다.It is a technique to prevent the breakdown of the solid fuel obtained through the nozzle by applying a twist to the waste passing through the nozzle to complicate the coupling structure between the components of the waste.

이와 같은 상기 종래의 가연성 쓰레기를 이용한 고체연료 성형기술은 종이류, 섬유류 합성수지류 등을 소정의 크기로 분쇄하고 그 분쇄된 가연성 쓰레기를 결합구조가 불규칙적이고 복잡화 되도록 가압하여 고체화시키는 단순한 기술로서 이는 폐기물만을 사용하는 것이 아니고 제지분야에서 재활용할 수 있는 종이류 까지도 같이 사용되어 부가가치 면에서 효율이 현저히 저하되는 문제점이 있다.The conventional solid fuel forming technology using the combustible waste as described above is a simple technique of pulverizing papers, fibers, synthetic resins, etc. to a predetermined size and pressurizing the pulverized combustible waste so that the bonding structure becomes irregular and complicated, which is solid waste only. There is a problem in that the efficiency of the added value is significantly reduced in that it is not used but also papers that can be recycled in the paper industry.

또 종래의 가연성 쓰레기를 이용한 고체연료 성형기술은 섬유류 합성수지류를 정제처리하지 않고 그냥 사용하기 때문에 연료로서 사용할 때에 발화되면서 대기오염은 물론 인체에 유해한 질산, 황산, 다이옥신, 염화수소 산화물 등이 대기 중에 그대로 방출됨으로 별도의 상기 유해성분 처리장치를 설치해야 하는 문제점이 있고 그에 따른 경제성에 문제가 있었다.In addition, the conventional solid fuel molding technology using combustible waste is used as a fuel without refining the synthetic resins, so it is ignited when used as a fuel, so that nitrates, sulfuric acid, dioxins, and hydrogen chloride oxides, which are harmful to the air as well as harmful to the human body, remain in the air There is a problem in that the installation of the separate hazardous component processing apparatus has been released and there was a problem in the economy accordingly.

또한 상기 종래의 가연성 쓰레기를 이용한 고체연료는 억지로 가압 성형된 상태임으로 운반도중 파손될 염려가 있고, 특히 우천시 또는 취급 부주의로 인하여 종이류에 수분이 흡수되면 그 흡수된 수분을 건조하여 사용해야 함으로 많은 시간과 노력이 필요하였다.In addition, the conventional solid fuel using the combustible waste is forcibly pressurized and may be damaged during transportation. In particular, when water is absorbed in papers due to rainy weather or careless handling, the absorbed moisture should be dried and used for a long time and effort. Was needed.

본 발명은 상기와 같은 제반 문제점을 감안하여 이를 해소하고자 발명한 것으로서, 이는 산업폐기물이라 할 수 있는 폐합성수지 즉 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS, 폐지 등을 이용하여 취급 및 보관이 용이하고 발열량이 높은 고체연료를 제조하여 제공함으로서 상기 폐합성수지를 재활용함과 동시에 환경오염을 방지하여 국가경제에 이바지할 수 있으며 에너지자원 부족현상을 해소할 수 있도록 함에 그 목적이 있다.The present invention has been invented to solve the above problems in consideration of the above problems, which uses waste synthetic resin, that is, waste synthetic fiber, waste synthetic rubber, waste PE, waste PP, waste PS, waste paper, etc., which can be called industrial waste. The purpose of the present invention is to manufacture and provide solid fuel, which is easy to handle and store, and to recycle the waste synthetic resin and to prevent environmental pollution, thereby contributing to the national economy, and to solve the shortage of energy resources. .

도 1은 본 발명의 폐합성수지를 이용한 고체연료 제조방법을 나타낸 공정도,1 is a process chart showing a solid fuel manufacturing method using the waste synthetic resin of the present invention,

도 2는 본 발명의 폐합성수지를 이용한 고체연료 제조시스템을 나타낸 개략도,Figure 2 is a schematic diagram showing a solid fuel production system using the waste synthetic resin of the present invention,

도 3은 본 발명의 폐합성수지를 이용한 고체연료 제조방법으로 제조된 고체연료를 나타낸 사시도.Figure 3 is a perspective view showing a solid fuel produced by a solid fuel production method using the waste synthetic resin of the present invention.

<도면의 주요부부에 대한 부호 설명><Description of Signs of Major Parts of Drawings>

10 : 저장호퍼 20 : 정량기10: storage hopper 20: meter

30 : 이송 컨베이어 40 : 수분배출 컨베이어30: transfer conveyor 40: moisture discharge conveyor

50 : 물 수집탱크 60 : 금속 선별기50: water collection tank 60: metal sorter

70 : 분쇄기 71 : 집진기70: grinder 71: dust collector

80 : 혼합기 81 : 첨가제 투입기80: mixer 81: additive injector

90 : 고체연료 성형기 91 : 가열수단90: solid fuel molding machine 91: heating means

92 : 노즐 93 : 압출공92 nozzle 93 extrusion hole

100 : 고체연료100: solid fuel

상기 목적을 달성하기 위한 본 발명의 폐합성수지를 이용한 고체연료 제조방법 및 그 방법으로 제조된 고체연료의 특징적인 기술적 구성을 설명하면 다음과 같다.Hereinafter, a method for producing a solid fuel using the waste synthetic resin of the present invention and a characteristic technical configuration of the solid fuel produced by the method for achieving the above object are as follows.

본 발명의 폐합성수지를 이용한 고체연료 제조방법은 폐합성수지의 수분을 걸러내고 그 수분이 걸어진 폐합성수지로부터 비 인화성물질을 선별하는 공정; 상기 비 인화성물질이 선별된 폐합성수지를 분쇄기를 이용하여 분쇄하는 공정; 상기 분쇄된 폐합성수지에 취기, NOx, SOx, 다이옥신, 염화수소 산화물 등의 유해성분을 저감시키고 열 크래킹 현상을 제거하는 첨가제를 투입하여 혼합하는 공정; 상기 첨가제가 투입되어 혼합된 폐합성수지를 고체연료 성형기에 투입하여 열을 가하며 성형하여 외부로 배출시키는 공정; 상기 성형 완료되어 배출되는 폐합성수지의 성형물을 원하고자하는 크기로 절단하는 공정; 을 포함하는 것으로 이루어진다.Solid fuel production method using the waste synthetic resin of the present invention comprises the steps of filtering out the moisture of the waste synthetic resin and selecting the non-flammable material from the waste synthetic resin with the moisture; Pulverizing the waste synthetic resin in which the non-flammable substance is selected using a pulverizer; Adding and mixing additives for reducing harmful components such as odor, NOx, SOx, dioxin, and hydrogen chloride oxide to the pulverized waste synthetic resin and removing thermal cracking phenomenon; Injecting the waste synthetic resin mixed with the additives into a solid fuel molding machine, applying heat and molding the waste synthetic resin; Cutting the molded product of the waste synthetic resin discharged after completion of molding to a desired size; It consists of including.

한편 상기 폐합성수지는 폐합성섬유, 폐합성고무, 폐PE, 폐PP, 폐PS, 폐지 중 어느 하나 또는 2가지 이상이 혼합된 것이고, 상기 수분과 비 인화성 물질이 선별된 폐합성수지에 투입되는 첨가제는 산화칼슘, 합성 제올라이트이며, 상기 폐합성수지와 첨가제의 혼합비는 중량%로 폐합성섬유 2∼10%, 폐합성고무 2∼10%, 폐지 4∼15%, 폐PE 20∼30%, 폐PP 20∼30%, 폐PS 20∼30%, 산화칼슘 1∼2.5%, 합성 제올라이트 1∼2.5%이다.Meanwhile, the waste synthetic resin is any one or two or more of waste synthetic fibers, waste synthetic rubber, waste PE, waste PP, waste PS, waste paper, and mixed with the waste and the non-flammable material. Is calcium oxide and synthetic zeolite, and the mixing ratio of the waste synthetic resin and the additive is 2% by weight of waste synthetic fiber, 2-10% of waste synthetic rubber, 4-15% of waste paper, 20-30% of waste PE, and waste PP. 20-30%, spent PS 20-30%, calcium oxide 1-2.5%, synthetic zeolite 1-2.5%.

또 상기 분쇄기를 이용한 폐합성수지의 분쇄 크기는 길이 3∼10mm, 직경 1∼5mm 이고, 상기 고체연료 성형기에서의 폐합성수지 가열온도는 150∼200℃이며, 상기 고체연료 성형기에서 성형되어 배출되는 폐합성수지의 절단된 크기는 길이 5∼60mm, 직경 5∼40mm이다.In addition, the pulverization size of the waste synthetic resin using the pulverizer is 3 ~ 10mm in length, 1 ~ 5mm in diameter, the waste synthetic resin heating temperature in the solid fuel molding machine is 150 ~ 200 ℃, waste synthetic resin molded and discharged from the solid fuel molding machine The cut size is 5 to 60 mm in length and 5 to 40 mm in diameter.

또한 본 발명의 폐합성수지로 제조된 고체연료는 폐합성수지를 이용하여 고체연료를 형성함에 있어서, 상기 고체연료는 폐 합성섬유, 폐 합성고무, 폐지, 폐PE, 폐PP, 폐PS 중 어느 하나 또는 2가지 이상에 산화칼슘, 합성 제올라이트가 첨가제로 투입되어 혼합된 것이다.In addition, in the solid fuel prepared from the waste synthetic resin of the present invention to form a solid fuel using the waste synthetic resin, the solid fuel is any one of waste synthetic fibers, waste synthetic rubber, waste paper, waste PE, waste PP, waste PS or At least two kinds of calcium oxide and synthetic zeolite are added as additives and mixed.

그리고 상기 폐합성수지와 첨가제의 혼합비는 중량%로 폐합성섬유 2∼10%, 폐합성고무 2∼10%, 폐지 4∼15%, 폐PE 20∼30%, 폐PP 20∼30%, 폐PS 20∼30%, 산화칼슘 1∼2.5%, 합성 제올라이트 1∼2.5%이고, 상기 고체연료는 길이 5∼60mm, 직경 5∼40mm인 원주상 펠렛(Pellet)이다.In addition, the mixing ratio of the waste synthetic resin and the additive is 2% by weight of waste synthetic fiber, 2-10% of waste synthetic rubber, 4-15% of waste paper, 20-30% of waste PE, 20-30% of waste PP, and waste PS. 20 to 30%, calcium oxide 1 to 2.5%, synthetic zeolite 1 to 2.5%, and the solid fuel is a cylindrical pellet having a length of 5 to 60 mm and a diameter of 5 to 40 mm.

상기와 같은 특징을 갖는 본 발명의 폐합성수지를 이용한 고체연료 제조방법 및 그 방법으로 제조된 고체연료를 첨부도면을 참조하여 상세하게 설명하면 다음과 같다.The solid fuel production method using the waste synthetic resin of the present invention having the above characteristics and the solid fuel produced by the method will be described in detail with reference to the accompanying drawings.

도 1은 본 발명의 폐합성수지를 이용한 고체연료 제조방법을 나타낸 공정도이고, 도 2는 본 발명의 폐합성수지를 이용한 고체연료 제조시스템을 나타낸 개략도이며, 도 3은 본 발명의 폐합성수지를 이용한 고체연료 제조방법으로 제조된 고체연료를 나타낸 사시도로서,1 is a process chart showing a solid fuel production method using the waste synthetic resin of the present invention, Figure 2 is a schematic diagram showing a solid fuel production system using the waste synthetic resin of the present invention, Figure 3 is a solid fuel using the waste synthetic resin of the present invention As a perspective view showing a solid fuel produced by the manufacturing method,

본 발명은 도 1 및 도 2에 나타낸 바와 같이 폐합성수지를 이용한 고체연료 제조방법을 각 단계별로 설명하면 다음과 같다.1 and 2 as follows, the solid fuel manufacturing method using waste synthetic resin as described in each step as follows.

[제1단계][Step 1]

먼저 수집된 폐합성수지인 폐합성섬유, 폐합성고무, 폐지, 폐PE, 폐PP, 폐PS를 운송수단인 화물차 등을 이용하여 목적지(고체연료 제조공장)에 이송하여 각각의 저장호퍼(10)에 저장한다.First, each of the storage hoppers is transported to the destination (solid fuel manufacturing plant) by using waste synthetic fiber, waste synthetic rubber, waste synthetic rubber, waste paper, waste PE, waste PP, waste PS, etc. Store in

[제2단계][Step 2]

상기 각각의 저장호퍼(10)에 저장된 폐합성수지를 정량기(20)에 공급하고 그 공급된 정량기(20)가 원하고자 하는 량만큼 정량 되면, 그를 이송 컨베이어(30)로 배출하여 스크린체로 된 수분배출 컨베이어(40)로 이송시킨다.When the waste synthetic resin stored in each of the storage hopper 10 is supplied to the quantifier 20 and the supplied quantifier 20 is quantified as desired, it is discharged to the transfer conveyor 30 to form a screen. Transfer to the water discharge conveyor 40.

[제3단계][Step 3]

스크린체로 된 수분배출 컨베이어(40)로 이송된 폐합성수지는 진행도중 수분은 저부로 배출되어 물 수집탱크(50)에 모아지고, 상기 수분배출 컨베이어(40)의 출 측에 마련된 금속 선별기(60)에서는 금속성분을 선별하게 된다.The waste synthetic resin transferred to the water discharge conveyor 40 made of a screen body is discharged to the bottom while the water is being processed and collected in the water collection tank 50, and the metal sorter 60 provided on the exit side of the water discharge conveyor 40. In the metal component is selected.

단 상기 금속 선별기(60)는 자석으로서 폐합성수지 중에 혼합되어 이송되는 Fe(철)성분을 선별해내는 것인 바, 그 이유는 상기 금속이 폐합성수지와 함께 분쇄기(70)에 들어가면 그 분쇄기(70)가 훼손될 염려가 있음으로 그를 예방하기 위함이고, 또 하나는 상기 금속성분을 회수하여 재활용할 수 있도록 하기 위함이다.However, the metal sorter 60 selects the Fe (iron) component that is mixed and transported in the waste synthetic resin as a magnet because the metal enters the grinder 70 together with the waste synthetic resin. ) Is to prevent it from being damaged, and another is to recover and recycle the metal component.

그리고 상기 금속 선별기(60)로부터 회수된 금속은 회수하여 금속재활용 공장으로 보낸다.And the metal recovered from the metal sorter 60 is recovered and sent to the metal recycling plant.

[제4단계][Step 4]

상기 수분배출 컨베이어(40)로 이송되면서 수분이 배출되고 금속성분이 선별된 폐합성수지는 분쇄기(70)에 공급되고 그 분쇄기(70)내로 공급된 폐합성수지는 분쇄기(70)의 작동과 함께 길이 3∼10mm, 직경 1∼5mm가 되게 분쇄되면서 혼합기(80)에 공급한다.The waste synthetic resin in which water is discharged and the metal component is selected while being transferred to the moisture discharging conveyor 40 is supplied to the grinder 70, and the waste synthetic resin supplied into the grinder 70 is operated with the operation of the grinder 70. It is supplied to the mixer 80 while being pulverized to ˜10 mm and a diameter of 1 to 5 mm.

단 상기 분쇄기(70)에는 집진기(71)가 마련되어 있는데, 그 집진기(71)를 마련한 이유는 상기 폐합성수지를 분쇄하면서 발생하는 각종 분진을 대기 중에 방출시키지 않고 흡수하여 처리함으로서 대기오염을 방지하고자 하는 것이다.However, the grinder 70 is provided with a dust collector 71. The reason for providing the dust collector 71 is to prevent air pollution by absorbing and treating various dusts generated while grinding the waste synthetic resin in the atmosphere without release. will be.

또한 상기 폐합성수지를 길이 3∼10mm, 직경 1∼5mm가 되게 분쇄하는 이유는 후 공정에서 이루어지는 고체연료 성형 작업시 가열수단(91)에 의해 용이하게 가열되어 용융될 수 있도록 하기 위함이고, 상기 절단된 폐합성수지의 크기가 길이 3∼10mm, 직경 1∼5mm 보다 크게되면 용융시간이 길어지고 그에 따른 작업지연과 생산성저하의 원인이 된다.Further, the reason why the waste synthetic resin is pulverized to have a length of 3 to 10 mm and a diameter of 1 to 5 mm is so that the waste synthetic resin can be easily heated and melted by the heating means 91 during the solid fuel forming operation performed in a later step. When the size of the used waste synthetic resin is larger than 3 to 10 mm in length and 1 to 5 mm in diameter, the melting time becomes longer, resulting in delays in work and productivity.

[제5단계][Step 5]

상기 분쇄기(70)에 의해 분쇄된 폐합성수지 즉 폐합성섬유, 폐합성고무, 폐지, 폐PE, 폐PP, 폐PS 중 어느 하나 또는 2가지 이상이 투입되어 혼합되고, 또 혼합기(80)상에 마련된 첨가제 투입기(81)에서는 산화칼슘(CaO), 합성 제올라이트(X-Type Zeolite)를 첨가제로 투입하여 혼합한다.The waste synthetic resin pulverized by the crusher 70, that is, waste synthetic fibers, waste synthetic rubber, waste paper, waste PE, waste PP, waste PS, or any one or two or more of them are added and mixed, and then mixed on the mixer 80. In the prepared additive injector 81, calcium oxide (CaO) and synthetic zeolite (X-Type Zeolite) are added as additives and mixed.

한편 상기 폐합성수지에 첨가제로 산화칼슘(CaO) 및 합성 제올라이트를 첨가하는 이유는 상기 폐합성수지에서 발생하는 취기(臭氣), 질산(NOx), 황산(SOx), HCl, 산화물 등의 유해성분을 없애기 위함이며, 상기 산화칼슘 및 합성 제올라이트에 의해 Ca 성분은 CaCl2로 중화되어 다이옥신의 생성량이 적어지며 S 성분은 CaSO4화되어 저감된다. 이의 화학반응식은 하기와 같다.Meanwhile, the reason for adding calcium oxide (CaO) and synthetic zeolite as an additive to the waste synthetic resin is to remove harmful components such as odor, nitric acid (NOx), sulfuric acid (SOx), HCl, oxide, etc. generated from the waste synthetic resin. In order to eliminate, the Ca component is neutralized by CaCl 2 by the calcium oxide and the synthetic zeolite to reduce the amount of dioxins produced, and the S component is reduced by CaSO 4 . Its chemical reaction formula is as follows.

[화학반응식][Chemical Reaction Formula]

Ca(OH)2+ 2HCl →CaCl2+ 2H2OCa (OH) 2 + 2HCl → CaCl 2 + 2H 2 O

Ca(OH)2+ SOxl →CaSOx+1+ H2OCa (OH) 2 + SOxl → CaSOx +1 + H 2 O

그리고 상기 합성 제올라이트는 질산(NOx), 황산(SOx), HCl 등을 분자체로 흡착하여 고체연료의 연소시 무해화시키는 역할을 하며 폐합성수지의 분해율을 높여 안정적인 연소가 되게 함으로서 열 크래킹(Creaking)형상을 없애준다.In addition, the synthetic zeolite absorbs nitric acid (NOx), sulfuric acid (SOx), HCl, etc. with a molecular sieve, and serves to detoxify the combustion of solid fuel, and increases the decomposition rate of the waste synthetic resin to make stable combustion. Eliminates

또 상기 각각의 폐합성수지와 첨가제의 혼합 비율은 중량%로 폐 합성섬유 2∼10%, 폐 합성고무 2∼10%, 폐지 4∼15%, 폐PE 20∼30%, 폐PP 20∼30%, 폐PS 20∼30%, 산화칼슘 1∼2.5%, 합성 제올라이트 1∼2.5%인데, 상기 폐합성수지의 혼합비율이 그 이상이거나 그 이하가 되면 고체연료가 지녀야할 발열량이 목표치에 미치지 못함으로 하기에서 설명되는 실시 예에 의하여 결정하였다.In addition, the mixing ratio of each of the waste synthetic resins and the additives in weight% is 2-10% of waste synthetic fibers, 2-10% of waste synthetic rubber, 4-15% of waste paper, 20-30% of waste PE, and 20-30% of waste PP. , Waste PS 20-30%, calcium oxide 1-2.5%, synthetic zeolite 1-2.5%, if the mixing ratio of the above-mentioned synthetic resin is higher or lower, the calorific value of solid fuel does not reach the target value. Determined by the examples described in.

그리고 첨가제로 산화칼슘과 합성 제올라이트를 각각 중량%로 1∼2.5%를 사용하였는데, 그 이유는 상기에서 설명하였듯이 폐합성수지가 연소되면서 발생하는 악취 즉 취기와 대기오염의 결정적인 역할을 하는 질산(NOx), 황산(SOx), 염화수소(HCl), 산화물 등을 저감시키기 위함이며, 상기 첨가제의 사용량이 그 이하이면 취기, 질산, 황산, 염화수소, 산화물 등을 저감효과가 기대치에 미치지 못하고, 그 이상이면 효과는 좋으나 발열량이 떨어지는 문제점이 있다. 따라서 첨가제의 사용량은 산화칼슘, 합성 제올라이트 모두 중량%로 1∼2.5%의 사용함이 적당하다.In addition, 1 to 2.5% by weight of calcium oxide and synthetic zeolite were used as additives, as described above, because the odor generated by burning waste synthetic resin, namely nitrate (NOx), which plays a decisive role in odor and air pollution. , Sulfuric acid (SOx), hydrogen chloride (HCl), oxides, etc. to reduce, if the amount of the additive is less than the odor, nitric acid, sulfuric acid, hydrogen chloride, oxides, etc., the effect is less than expected, if the effect is higher than It is good but there is a problem that the heating value falls. Therefore, the amount of the additive is suitable to use 1% to 2.5% by weight of both calcium oxide and synthetic zeolite.

[제6단계][Step 6]

상기 혼합기(80)에 의해 폐합성수지와 첨가제가 혼합되면 그를 고체연료 성형기(90)에 투입하고 그 투입된 폐합성수지에 열을 가하며 용융시켜 압출하는데, 이때 상기 고체연료 성형기(90)에 투입된 폐합성수지의 가열온도는 150∼200℃이다.When the waste synthetic resin and the additive are mixed by the mixer 80, the waste synthetic resin is added to the solid fuel molding machine 90, and the melted resin is extruded by applying heat to the injected waste synthetic resin. In this case, the waste synthetic resin put into the solid fuel molding machine 90 is extruded. Heating temperature is 150-200 degreeC.

폐합성수지의 가열온도를 150∼200℃로 하는 이유는 200℃ 이상이 되면 폐합성수지의 특성상 타버리거나 기화되는 문제점이 있고, 150℃ 이하가 되면 폐합성수지가 용융이 더디게 됨으로 고체연료 제조작업이 지연되는 문제점이 있다. 따라서 폐합성수지의 가열온도는 150∼200℃가 적당하다.The reason why the heating temperature of the waste synthetic resin is 150 to 200 ° C. is that when it is 200 ° C. or more, there is a problem that it is burned or vaporized due to the characteristics of the waste synthetic resin. There is a problem. Therefore, the heating temperature of the waste synthetic resin is suitable to 150 ~ 200 ℃.

또 본 발명의 고체연료 성형기(90) 출 측에는 폐합성수지가 용융되어 압출되는 압출공(93)이 형성된 노즐(92)이 설치되고 그 노즐(92)의 압출공(93)은 원형이며 직경이 5∼40mm인데, 그 이유는 고체연료를 원주상 펠렛으로 형성시키고 그 펠렛의 직경 크기를 5∼40mm로 하기 때문이다.In addition, a nozzle 92 having an extrusion hole 93 for melting and extruding waste synthetic resin is formed on the exit side of the solid fuel molding machine 90 of the present invention, and the extrusion hole 93 of the nozzle 92 has a circular shape and a diameter of 5 The reason is that the solid fuel is formed into columnar pellets and the diameter of the pellets is 5 to 40 mm.

단 상기 노즐(92)의 압출공(93) 형상은 상기에서 설명한 원형으로 한정하지 않고 적어도 3각 이상의 각형으로 형성시켜 사용해도 무방하고, 직경 역시 상기에서 설명한 5∼40mm가 아닌 사용 용도와 목적에 따라 다양한 크기로 형성시켜 사용해도 무방하다.However, the shape of the extrusion hole 93 of the nozzle 92 is not limited to the circular shape described above, but may be used to form at least three squares or more, and the diameter is also for use purposes and purposes other than 5 to 40 mm as described above. Therefore, it can be used in various sizes.

[제7단계][Step 7]

상기 고체연료 성형기(90)의 출 측에 마련된 노즐(92)의 압출공(93)을 통하여 압출되는 폐합성수지는 길이가 60mm 이하가 되게 절단 나이프를 이용하여 절단하고 건조하는데, 상기 압출되는 폐합성수지의 절단시기는 압출공(93)의 입 측에서 압출됨과 동시에 절단하거나 또는 일정량만큼 압출한 다음 그를 60mm 이하가 되게절단해도 된다.The waste synthetic resin extruded through the extrusion hole 93 of the nozzle 92 provided on the outlet side of the solid fuel molding machine 90 is cut and dried using a cutting knife to have a length of 60 mm or less, and the extruded waste synthetic resin The cutting timing of may be simultaneously extruded at the mouth side of the extrusion hole 93 or may be extruded by a predetermined amount and then cut to be 60 mm or less.

그리고 절단된 압출물의 건조는 상기 고체연료 성형기(90)의 가열수단(91)에 의해 가열된 상태로 압출되는 압출물을 냉각시키는 것을 의미하는 것으로서, 압출물이 냉각되면 폐합성수지의 특성상 단단한 고체상태로 변하게 되어 고체연료가 되는 것이다.In addition, drying of the cut extrudate means cooling the extrudate extruded in a heated state by the heating means 91 of the solid fuel molding machine 90. When the extrudate is cooled, a solid solid state due to the characteristics of the waste synthetic resin is cooled. To become solid fuel.

이상과 같이 제1단계 내지 제7단계의 과정을 거쳐 제조된 고체연료는 각종 건물의 난방용으로 사용하거나 공장의 보조연료 및 소각장의 소각연료 등으로 사용할 수 있으며, 대기오염 물질인 질산, 황산, 다이옥신, 염화수소, 산화물 등의 발생 농도가 현저하게 낮기 때문에 고도의 공해방지시설을 갖추지 않고도 사용할 수 있는 효과가 있다.As described above, the solid fuel manufactured through the first to seventh steps may be used for heating various buildings or as an auxiliary fuel of a factory and an incineration fuel of an incinerator, and the air pollutants such as nitric acid, sulfuric acid and dioxins Since the concentration of hydrogen chloride, oxides, etc. is remarkably low, it can be used without having a high pollution prevention facility.

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

[실시예1]Example 1

본 발명은 먼저 수분과 금속성분이 제거되고 분쇄기(70)를 통하여 길이 5mm, 직경 2.5mm로 분쇄된 폐합성수지 중 중량%로 폐합성섬유 10%, 폐합성고무 10%, 폐지15%, 폐PE 20%, 폐PP 20%, 폐PS 20%,산화칼슘 2.5%, 합성 제올라이트 2.5%를 혼합기(80)에 투입하여 혼합하고, 그 혼합된 폐합성수지를 고체연료 성형기(90)에 투입한 다음 상기 고체연료 성형기(90)의 가열수단(91)을 180℃로 가열하여 상기 투입된 폐합성수지를 용융시켜 압출시키고 그 압출되는 압출물을 길이 50mm가 되게 절단한 다음 건조하여 그를 보일러의 연료로 사용해본 결과 발열량이 600kcal/kg 이였고, 1톤의 물을 100℃ 이상이 되게 끊이는데 걸리는 사간은 15분이 걸렸다.In the present invention, first, water and metal components are removed, and the waste synthetic resin, which is pulverized to a length of 5 mm and a diameter of 2.5 mm through a grinder 70, by weight% of waste synthetic fiber 10%, waste synthetic rubber 10%, waste paper 15%, waste PE 20%, 20% waste PP, 20% waste PS, 2.5% calcium oxide, 2.5% synthetic zeolite were added to the mixer 80 and mixed, and the mixed waste synthetic resin was added to the solid fuel molding machine 90. The heating means 91 of the solid fuel molding machine 90 was heated to 180 ° C. to melt and extrude the injected waste synthetic resin, cut the extruded extrudate to a length of 50 mm, and dry it to use it as a fuel for a boiler. The calorific value was 600 kcal / kg, and the time it took to cut one ton of water above 100 ° C took 15 minutes.

[실시예2]Example 2

본 발명의 실시 예2는 상기 실시예1과 마찬가지로 수분과 금속성분이 제거되고 분쇄기(70)를 통하여 길이5mm, 직경 2,5mm로 분쇄된 폐합성수지를 중량%로 폐 합성섬유 5%, 폐 합성고무 7%, 폐지 15%, 폐PE 25%, 폐PP 25%, 폐PS 20%, 산화칼슘 1.5%, 합성 제올라이트 1.5%를 혼합기(80)에 투입하여 혼합하고 그 혼합된 폐합성수지를 고체연료 성형기(90)에 투입한 다음 상기 고체연료 성형기(90)의 가열수단(91)을 180℃로 가열하여 상기 투입된 폐합성수지를 용융시켜 압출시키고 그 압출되는 압출물을 길이 40mm가 되게 절단한 다음 건조하여 그를 소각장의 소각연료로 사용해본 결과 발열량이 590kcal/kg 이었고, 1톤의 소각물을 소각하는데 걸리는 시간은 10분이 걸렸다.Example 2 of the present invention is the waste synthetic resin 5% waste synthetic fiber in 5% by weight of waste and synthetic resin, which is pulverized to 5mm in length, 2,5mm in diameter by removing the water and metal components as in Example 1 Rubber 7%, waste paper 15%, waste PE 25%, waste PP 25%, waste PS 20%, calcium oxide 1.5%, synthetic zeolite 1.5% are added to the mixer 80, and the mixed waste synthetic resin is mixed with solid fuel. After input to the molding machine 90, the heating means 91 of the solid fuel molding machine 90 is heated to 180 ° C to melt and extrude the injected waste synthetic resin and cut the extruded extrudate to a length of 40mm and then dried He used it as an incineration fuel for incinerators, and the calorific value was 590 kcal / kg, and the time it took to incinerate one ton of incinerator took 10 minutes.

[실시예3]Example 3

본 발명의 실시예3은 상기 실시예1 및 실시예2와 마찬가지로 수분과 금속성분이 제거되고 분쇄기(70)를 통하여 길이 5mm, 직경 2.5mm로 분쇄된 폐합성수지를 중량%로 폐합성섬유 7%, 폐합성고무 10%, 폐지 10%, 폐PE 30%, 폐PP 20%, 폐PS 20%, 산화칼슘 1.5%, 합성 제올라이트 1.5%를 혼합기(80)에 투입하여 혼합하고 그 혼합된 폐합성수지를 고체연료 성형기(90)에 투입한 다음 상기 고체연료 성형기(90)의 가열수단(91)을 180℃로 가열하여 상기 투입된 폐합성수지를 용융시켜 압출시키고 그 압출되는 압출물을 길이 30mm가 되게 절단한 다음 건조하여 그를 비닐하우스의 난방연료로 사용해본 결과 발열량이 550kcal/kg 이었다.Example 3 of the present invention is a waste synthetic resin 7% by weight of waste synthetic resin pulverized to 5mm in length, 2.5mm in diameter by removing the water and metal components as in the first and second embodiments and the mill 70 , Waste synthetic rubber 10%, waste paper 10%, waste PE 30%, waste PP 20%, waste PS 20%, calcium oxide 1.5%, synthetic zeolite 1.5% was added to the mixer 80, and the mixed waste synthetic resin To the solid fuel molding machine (90) and then heating means (91) of the solid fuel molding machine (90) After heating to 180 ° C, the injected waste synthetic resin was melted and extruded, and the extruded extrudate was cut to have a length of 30 mm, dried, and used as a heating fuel of a vinyl house. The calorific value was 550 kcal / kg.

이상과 같은 방법에 의해 제조된 본 발명의 고체연료는 연소가 안정적으로 이루어지고 열 크래킹이 없으며 제조공정에서 불연물이 제거되고 분쇄되어 혼합, 압축 성형됨으로 조성가연성분이 균일하여 발열량이 매우 높아 열효율이 좋은 특유의 효과가 있다.Solid fuel of the present invention produced by the above method is stable combustion, there is no thermal cracking, non-combustibles are removed in the manufacturing process, pulverized, mixed, compression molding, the composition combustible components are uniform, the calorific value is very high heat efficiency is good Has a unique effect.

또 본 발명의 고체연료는 취급이 간편하여 연료가 필요한 곳이라면 어느 곳이나 용이하게 운반하여 사용할 수 있고, 사용범위가 제한 없이 광범위하게 사용할 수 있으며, 중화제인 산화칼슘과 합성 제올라이트를 첨가하여 제조함으로서 대기오염 물질이며 인체에 유해한 질산, 황산, 다이옥신, 산화물 등의 발생을 저감시킬 수 있는 특유의 효과가 있다.In addition, the solid fuel of the present invention can be easily transported and used wherever fuel is needed because it is easy to handle, and can be used in a wide range without limit of use, and is prepared by adding calcium oxide and synthetic zeolite, which are neutralizing agents. It is an air pollutant and has a unique effect of reducing the generation of nitric acid, sulfuric acid, dioxins, and oxides, which are harmful to the human body.

Claims (10)

폐합성수지의 수분을 걸러내고 그 수분이 걸어진 폐합성수지로부터 비 인화성물질을 선별하는 공정;Filtering water from the waste synthetic resin and separating non-flammable substances from the waste synthetic resin to which the moisture has been suspended; 상기 비 인화성물질이 선별된 폐합성수지를 분쇄기를 이용하여 분쇄하는 공정;Pulverizing the waste synthetic resin in which the non-flammable substance is selected using a pulverizer; 상기 분쇄된 폐합성수지에 취기, NOx, SOx, 다이옥신, HCl 산화물 등의 유해성분을 저감시키고 열 크래킹 현상을 제거하는 첨가제를 투입하여 혼합하는 공정;Adding and mixing additives for reducing harmful components such as odor, NOx, SOx, dioxin, HCl oxide and removing thermal cracking phenomenon into the pulverized waste synthetic resin; 상기 첨가제가 투입되어 혼합된 폐합성수지를 고체연료 성형기에 투입하여열을 가하며 성형하여 외부로 배출시키는 공정;Injecting the waste synthetic resin mixed with the additives into a solid fuel molding machine, applying heat to form the waste, and discharging it to the outside; 상기 성형 완료되어 배출되는 폐합성수지의 성형물을 원하고자하는 크기로 절단하는 공정; 을 포함함을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.Cutting the molded product of the waste synthetic resin discharged after completion of molding to a desired size; Solid fuel production method using a waste synthetic resin, characterized in that it comprises a. 제1항에 있어서, 상기 폐합성수지는 폐 합성섬유, 폐 합성고무, 폐지, 폐PE, 폐PP, 폐PS 중 어느 하나 또는 2가지 이상이 혼합된 것임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 1, wherein the waste synthetic resin is any one or two or more of waste synthetic fibers, waste synthetic rubber, waste paper, waste PE, waste PP, and waste PS are mixed. . 제1항에 있어서, 상기 수분과 비 인화성물질이 선별된 폐합성수지에 투입되는 첨가제는 산화칼슘, 합성 제올라이트임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 1, wherein the additive added to the waste synthetic resin in which the water and the non-flammable material are selected is calcium oxide and synthetic zeolite. 제2항 또는 제3항에 있어서, 상기 폐합성수지와 첨가제의 혼합비는 중량%로 폐합성섬유 2∼10%, 폐합성고무 2∼10%, 폐지 4∼15%, 폐PE 20∼30%, 폐PP 20∼30%, 폐PS 20∼30%, 산화칼슘 1∼2.5%, 합성 제올라이트 1∼2.5%임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 2 or 3, wherein the mixing ratio of the waste synthetic resin and the additive is 2% by weight of synthetic fiber 2-10%, 2-10% waste synthetic rubber, 4-15% waste paper, 20-30% waste PE, 20 to 30% of waste PP, 20 to 30% of waste PS, 1 to 2.5% of calcium oxide, and 1 to 2.5% of synthetic zeolite. 제1항에 있어서, 상기 분쇄기를 이용한 폐합성수지의 분쇄 크기는 3∼10mm, 직경 1∼5mm 임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 1, wherein the size of the waste synthetic resin using the mill is 3 to 10mm, diameter 1 to 5mm. 제1항에 있어서, 상기 고체연료 성형기에서의 폐합성수지 가열온도는 150∼200℃임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 1, wherein the waste synthetic resin heating temperature in the solid fuel molding machine is 150 ~ 200 ℃. 제1항에 있어서, 상기 고체연료 성형기에서 성형되어 배출되는 폐합성수지의 절단된 크기는 길이 5∼60mm, 직경 5∼40mm 임을 특징으로 하는 폐합성수지를 이용한 고체연료 제조방법.The method of claim 1, wherein the cut size of the waste synthetic resin molded and discharged from the solid fuel molding machine is 5 to 60 mm in length and 5 to 40 mm in diameter. 폐합성수지를 이용하여 고체연료를 형성함에 있어서, 상기 고체연료는 폐합성섬유, 폐합성고무, 폐지, 폐PE, 폐PP, 폐PS 중 어느 하나 또는 2가지 이상에 산화칼슘, 합성 제올라이트가 첨가제로 투입되어 혼합된 것임을 특징으로 하는 폐합성수지로 제조된 고체연료.In the formation of solid fuel using waste synthetic resin, the solid fuel may include calcium oxide and synthetic zeolite as additives in any one or two or more of waste synthetic fiber, waste synthetic rubber, waste paper, waste PE, waste PP, and waste PS. Solid fuel produced from waste synthetic resin, characterized in that the mixture is added. 제8항에 있어서, 상기 폐합성수지와 첨가제의 혼합비는 중량%로 폐합성섬유 2∼10%, 폐합성고무 2∼10%, 폐지 4∼15%, 폐PE 20∼30%, 폐PP 20∼30%, 폐PS 20∼30%, 산화칼슘 1∼2.5%, 합성 제올라이트 1∼2.5%임을 특징으로 하는 폐합성수지로 제조된 고체연료.The method of claim 8, wherein the mixing ratio of the waste synthetic resin and the additive is 2% by weight of waste synthetic fiber, 2-10% waste synthetic rubber, 4-15% waste paper, 20-30% waste PE, 20-20 waste PP. 30%, waste PS 20-30%, calcium oxide 1-2.5%, synthetic zeolite 1-2.5%. 제8항에 있어서, 상기 고체연료는 길이 5∼60mm, 직경 5∼40mm인 원주상 펠렛 임을 특징으로 하는 폐합성수지로 제조된 고체연료.9. The solid fuel of claim 8, wherein the solid fuel is columnar pellets having a length of 5 to 60 mm and a diameter of 5 to 40 mm.
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KR20020080541A (en) * 2001-04-16 2002-10-26 주식회사 명현엔지니어링 Method for making a refuse derived fuel
KR20030038884A (en) * 2001-11-07 2003-05-17 박금남 Hot air or hot water supplying apparatus and method for incinerating waste agricultural house vinyl fuel and its waste agricultural house vinyl fuel
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
KR101667359B1 (en) * 2015-07-03 2016-10-21 주식회사 브릿지오브날리지 Refuse Plastic Fuel, And Apparatus And Method for Manufactring the Same
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Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0688083A (en) * 1992-09-07 1994-03-29 Kunio Kato Production of solid fuel from combustible waste
JPH06108075A (en) * 1992-09-25 1994-04-19 Mitsubishi Heavy Ind Ltd Production 0f solid fuel from waste material
JPH0925489A (en) * 1995-07-10 1997-01-28 Toshiba Mach Co Ltd Production of solid fuel and solid fuel
KR0178336B1 (en) * 1996-09-10 1999-04-01 김형래 Method for producing solid fuel from waste, solid fuel moldings thereof, and operation of solid fuel combustion furnace
JPH10130672A (en) * 1996-10-25 1998-05-19 Hitachi Ltd Production of solid fuel
KR100390933B1 (en) * 1998-11-17 2003-10-04 주식회사 정토에너지 Solidified fuel using general waste

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KR20020080541A (en) * 2001-04-16 2002-10-26 주식회사 명현엔지니어링 Method for making a refuse derived fuel
KR20030038884A (en) * 2001-11-07 2003-05-17 박금남 Hot air or hot water supplying apparatus and method for incinerating waste agricultural house vinyl fuel and its waste agricultural house vinyl fuel
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
KR20020066315A (en) * 2002-07-24 2002-08-14 김수용 The Apparatus of Recycling Wastes for a Substitute Energy and the Manufacturing Process
KR101667359B1 (en) * 2015-07-03 2016-10-21 주식회사 브릿지오브날리지 Refuse Plastic Fuel, And Apparatus And Method for Manufactring the Same
WO2017213395A1 (en) * 2016-06-07 2017-12-14 김선석 Method for preparing solid-phase raw material using waste fibers
KR20200132649A (en) 2019-05-17 2020-11-25 김용학 Fuel pellet containing cotton waste and a preparing method thereof
KR20210095451A (en) * 2020-01-23 2021-08-02 가세진 Method for recycling waste rubber and recycled rubber therefrom

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