• 제목/요약/키워드: Gasification melting

검색결과 35건 처리시간 0.025초

PGV(Plasma Gasification & Vitrification) 시스템을 통한 폐기물의 자원화 기술 (A Study on Recycling Technology of Wastes by Using PGV(Plasma Gasification & Vitrification) System)

  • 유대우;김영석
    • 플랜트 저널
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    • 제4권4호
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    • pp.62-70
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    • 2008
  • PGV(Plasma Gasification & Vitrification) system has been developed based on a pyrolysis melting gasification technology that provides the possibilities of acquiring renewable energy. As volume of wastes increases with the rapid industrialization and population growth, eco friendly disposal is drawing more social attention. Pyrolysis plasma technology is regarded as the best environmentally friendly process for the waste disposal among numerous waste disposal processes. Introduced in this paper is the behavior of the plasma torch and a computational fluid simulation dynamics is discussed for designing the melting furnace. Some PGV applications have also been discussed.

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Fundamental study on development of latent heat storage material for waste heat recovery of biomass gasification

  • Kim, MyoungJun;Yu, JikSu;Chea, GyuHoon
    • Journal of Advanced Marine Engineering and Technology
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    • 제38권5호
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    • pp.533-540
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    • 2014
  • Recently, latent heat thermal energy storage system (LHTES) has gained attention in order to utilize middle temperature (373~573 K) waste heat from biomass gasification. This paper has investigated thermo-physical properties of erythritol [$CH_2OHCHOH$ $CHOHCH_2OH$], mannitol [$CH_2OH$ $(CHOH)_4CH_2OH$] and their compounds as phase change materials (PCMs). The differential scanning calorimetry (DSC) was applied to measure the melting point and latent heat of these PCMs. Also the melting and solidification characteristics of these PCMs were observed in a glass tube with a digital camera. In the DSC measurement, when the amount of mannitol content was more than 40 mass%, the melting point of these compounds show two melting points. The experimental results showed that the velocity of melting and solidification were different for every mixture ratio of compounds. These compounds had the super-cooling phenomenon during the solidification process.

5톤/일 shaft형 pilot plant에서 자동차 폐차 잔재의 가스화 용융 특성 (Gasification melting characteristics of Automobile shredder residue in 5t/d shaft pilot plant)

  • 노선아;김우현;윤진한;홍병권
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2010년도 추계학술대회 초록집
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    • pp.160-160
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    • 2010
  • ELVs (End-of-Vehicles) in Korea incrasease continusely because of increase of used car. Automobile Shredder Residue (ASR) is final product of ELVs (End-of-Vehicles) after recycling. Automobile Shredder Residue are composed of light and heavy fluffs and soil/dust. In this study, 5 ton/day pilot plant of shaft type has been designed and constructed and 15 times of test run were performed. For the stable operation, operation conditions such as the amount of fed ASR and cokes, air flow and temperature in the gasification melting system have been changed and the composition of the produced gas such as $H_2$, CO and $CH_4$ and air pollution compound including dioxin discharged from the stack have been analyzed.

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생활폐기물 열분해-가스화-용융공정시설에서 다이옥신의 분포특성 (Distribution characteristics of dioxin concentration in pyrolysis-gasification-melting process facilities)

  • 손지환;김기헌;강영렬;박선구
    • 분석과학
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    • 제20권1호
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    • pp.10-16
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    • 2007
  • 생활폐기물 열분해-가스화-용융공정 2개 시설(A 및 B 시설)에 대하여 PCDDs/PCDFs 농도를 조사한 결과, A시설은 2차연소로후단, 보일러후단, 굴뚝에서 PCDDs/PCDFs의 농도는 각각 0.88, 2.29, 0.16 ng I-TEQ/$m^3$으로 나타났다. B시설에서 열분해-가스화-용융로후단, 굴뚝에서 PCDDs/PCDFs 농도는 각각 0.22, 0.05 ng I-TEQ/$m^3$로 나타났다. 두 시설 모두에서 고온의 연소로보다 냉각구간의 보일러에서 다이옥신의 재합성으로 인하여 농도가 증가되었다. 또한 A시설에서는 2, 3, 4, 7, 8-PeCDF, 2, 3, 4, 6, 7, 8-HxCDF, 1, 2, 3, 6, 7, 8-HxCDF 순서로 높은 농도를 나타냈으며, B시설은 2, 3, 4, 7, 8-PeCDF, 1, 2, 3, 7, 8-PeCDD, 2, 3, 4, 6, 7, 8-HxCDF 순서로 높게 나타났다.

열분해 가스화 용융시스템에서 용융슬래그의 폐열 활용 (Waste Heat Utilization of Melted slags at Pyrolysis, Gasification and Melting System)

  • 이호석;성상철;오명도
    • 대한설비공학회:학술대회논문집
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    • 대한설비공학회 2008년도 하계학술발표대회 논문집
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    • pp.1237-1242
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    • 2008
  • A study on waste heat utilization of melted slags at pyorlysis, gasification and melting system was performed. Researchers studied heat balance of substances that flow and flow out to the system which is consisted of melting furnace, combustion chamber, and waste heat boiler, then they calculated melting slags' quantity of heat by the first law of thermodynamics. If they use water cursh pit outflow which is gotten by quenching of melting slag as a energy for heating and cooling system, steam of waste heat boiler would be delivered to a steam turbine, making energy, then they will get 67,671,000 won of profit a year. It will take 3 years to repossess the cost that they invested for building it. And, if we predict durability of trash burner is 20 years, we will get approximately 1,150,407,000 won of profits in 17 years without the period when we repossess the building costs.

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플라즈마 방식 열분해 가스화용융시설의 공정별 클로로벤젠 및 클로로페놀 배출거동에 관한 연구 (A Study on the Chlorobenzene and Chlorophenol Behavior in Plasma Type Pyrolysis/Gasfication/Melting Process)

  • 신찬기;신대윤;김기헌;손지환
    • 환경위생공학
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    • 제22권2호
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    • pp.9-20
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    • 2007
  • The incineration process has commonly used for wastes amount reduction and thermal treatments of pollutants as the technologies accumulated. However, the process is getting negative public images owing to matter of hazardous pollutants emission. Specially dioxins became a main issue and were mostly emitted from municipal solid wastes incineration. In this reason, pyrolysis/gasification/melting process is presented as an alternative of incineration process. The pyrolysis/gasification/melting process, a novel technology, is middle of verification of commercial plant and development of technologies in Korea. But the survey about the pollutant emission from the process, and background data in these facilities is necessary. So in this survey, t is investigated that the behavior of chlorobenzenes and chlorophenols in plasma type pyrolysis/gasification/melting plant of pilot scale. We investigated discharging behavior of each phase of chlorobenzene through each process in the plsasma type pyrolysis/gasification/melting process. From this result, it was found that about 99 percent of particle-phase chlorobenzene was removed, but on the other hand gas-phase chlorobenzene was increased by about 600 percent through heat exchanger, flue gas cooling, system and semi dry absorption bag filter(SDA/BF). Also, this investigation presented that di-chlorobenzene(DCB) tri-chlorobenzene(TCB), tetra-chlorobenzene(TeCB), penta-chlorobenzene (PCB), except mono-chlorobenzene(MCB) and hexa-chlorobenzene(HCB) were increased through the flue gas cooling system and the semi dry absorption bag filter(SDA/BF). It was investigated that concentration of particle-phase chlorophenol was decreased by about 66 percent, but on the other hand, concentration of gas-phase chlorophenol was increased by about 170 percent through heat exchanger, flue gas cooling system, and semi dry absorption bag filter(SDA/BF). Also, it was found that di-chlorophenol(DCP), tri-chlorophenol(TCP), and penta-chlorophenol(PCP) were increased through the flue gas cooling system, and the semi dry absorption bag filter(SDA/BF). It can be considered that small-scale pilot facility and short investigation period might cause the concentration increase through the flue gas cooling system and the semi dry absorption bag filter(SDA/BF). A further study on real-scale pilot facility and accurate investigation may be required.