• 제목/요약/키워드: Solid particle

검색결과 1,025건 처리시간 0.024초

탄재를 포함한 산화철 펠릿 소성 공정 수치 모델의 입자 반응 모델 적용 (A discussion on the application of particle reaction model for iron ore pellet induration process modeling)

  • 안형준;최상민
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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    • pp.165-166
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    • 2014
  • The application of particle reaction model in the packed bed process modeling is discussed for iron ore pellet induration process. Combustion of coke breeze in the pellet is estimated by using shrinking unreacted-core model and grain model in which the progress of chemical reaction is described in different concepts. Under the identical inlet gas and solid conditions, the calculation using shrinking core model showed deviated results in terms of temperature profile and conversion fraction, which may imply the significance of selecting proper particle reaction model in consideration of particle characteristics and process operation conditions.

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싸이클론 집진기의 수치해석적 연구 (Numerical Study of Cyclone Dust Collector)

  • 전영남;엄태인
    • 한국대기환경학회지
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    • 제12권1호
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    • pp.43-53
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    • 1996
  • Numerical simulation was performed for the 3-dimensional flow filed of gas and particle phase for cyclone dust collector. FVM(Finite Volume Method) was employed for gas phase. The flow was solved suing the k-.varepsilon. epsilon turbulence model. The particle exit at the bottom of the cone was treated as a solid wall in this model because the gas flow through the effective dust exit is usually insignificant. The major parameters considered in this study was vortex finder diameter, effective dust exit diameterm vortex finder length, inlet type for dimension performance. Particle trajectory calculations were made for three different, particle sizes of 1, 25 and 50 .mu.m. The results obtained from this study give some physical insight of dust particle collection mechanism together with the indication of the collection efficiency. The simulation results were in generally good agreement with empirical knowledge. The application of this kind of computer program looks promising as a potential tool for the design of cyclone and determination of optimum operating condition.

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과공정 Al- Si 합금의 반응고 교반시 초정 Si 형상에 미치는 교반조건 및 개량원소 첨가 영향 (Effects of Stirring Condition and Refining Element Addition on the Primary Si Particle Morphology of Hypereutectic Al-Si Alloys Semi-Solid State Processing)

  • 김인준;김도향
    • 한국주조공학회지
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    • 제18권5호
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    • pp.474-480
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    • 1998
  • Microstructural characteristics of semi-solid state processed hypereutectic Al-Si alloys have been investigated. Main concern of the present study is to investigate the effects of P and Sr addition on the size and morphology change of the primary Si particles. Refinement of the primary Si particles was observed with the addition of P and Sr at the early stage of semi-solid state processing, but such a refining effects became negligible resulting in Si particles with a near-spherical morphology with continuous stirring. This implies that the microstructural transformation mechanism became more dependent to stirring effects than to the alloying effects during semi-solid state processing. Brittle fracture and agglomeration were proposed as the mechanisms for microstructural alterations during semi-solid state processing.

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순환유동층에서 Solid Mass Inventory에 따른 수력학적 특성 연구 (Hydrodynamic Characteristics of Circulating Fluidized Bed in Different Mass Inventories)

  • 김은경;신동훈;황정호;이종민;김재성
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2002년도 제25회 KOSCI SYMPOSIUM 논문집
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    • pp.165-172
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    • 2002
  • This paper discusses hydrodynamic characteristics of cold circulating fluidized bed(CFB) in different solid mass inventories. Operating parameters of solid mass inventory, primary air and J-valve fluidizing air were varied to find out the effect on the flow fludization pattern. Experimental measurements were made in a 3m tall CFB that has 0.05m riser diameter and black silica-carbonate of particle sizes from $100{\mu}m$ to $500{\mu}m$ were employed as the bed material. The operating conditions of superficial gas velocity and J-valve fluidizing velocity were in the ranges of 1.39~3.24 m/s and 0.139~0.232 m/s respectively. The axial solid fraction and solid circulation rate of CFB were observed and compared with modelling through IEA-CFBC Model and commercial CFD code.

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固體粉末이 浮上된 二相亂流 管流動의 熱傳達에 관한 硏究 (Study on the two phase turbulent heat transfer of gas-solid supension flow in pipes)

  • 김재웅;김봉기;최영돈
    • 대한기계학회논문집
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    • 제13권3호
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    • pp.528-537
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    • 1989
  • The objective of this paper is to investigate effects of the specific heat and the diameter of suspending particles on the heat transfer coefficient of two phase turbulent flow with suspension of solid particles in a circular tube with constant heat flux. Heat transfer coefficients of two phase turbulent flow in pipe with suspension of graphite powder were measured with variations of particle sizes and solid-gas loading ratio. Measured data were compared with predictions by numerical analysis in which the turbulece models are closed on the first order level. Results show that heat transfer coefficient increases with increasing the solid-gas loading ratio and the specific heat of suspending material, however, it decreases as the average diameter of particles decreases below $24{\mu}m$.

고체분산체를 이용한 약물의 생체이용율 향상을 위한 전략 (Solid Dispersion as a Strategy to Improve Drug Bioavailability)

  • 박준형;전명관;조훈;최후균
    • KSBB Journal
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    • 제26권4호
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    • pp.283-292
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    • 2011
  • Solid dispersion is one of well-established pharmaceutical techniques to improve the dissolution and consequent bioavailability of poorly water soluble drugs. It is defined as a dispersion of drug in an inert carrier matrix. Solid dispersions can be classified into three generations according to the carrier used in the system. First and second generations consist of crystalline and amorphous substances, respectively. Third generation carriers are surfactant, mixture of polymer and surfactants, and mixture of polymers. Solid dispersions can be generallyprepared by melting method and solvent method. While melting method requires high temperature to melt carrier and dissolve drug, solvent method utilizes solvent to dissolve the components. The improvement in dissolution through solid dispersions is attributed to reduction in drug particle size, improvement in wettability, and/or formation of amorphous state. The primary characteristics of solid dispersions, the presenceof drug in amorphous state, could be determined by differential scanning calorimetry (DSC), powder X-ray diffraction (PXRD), and fourier-transformed infrared spectroscopy (FTIR). In spite of the significant improvement in dissolution by solid dispersion technique, some drawbacks have limited the commercial application of solid dispersions. Thus, further studies should be conducted in a direction to improve the congeniality to commercialization.

Characteristics of Fluid Flow in the Fluidized Bed Shell and Tube Type Heat Exchanger with Corrugated Tubes

  • Ahn Soo Whan;Bae Sung Taek;Kim Myoung Ho
    • International Journal of Air-Conditioning and Refrigeration
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    • 제12권4호
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    • pp.198-205
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    • 2004
  • An experimental study was carried on the characteristics of fluid flow and heat transfer in a fluidized bed shell-and-tube type heat exchanger with corrugated tubes. Seven different solid particles having same volume were circulated in the tubes. The effects of vari­ous parameters such as water flow rates, particle geometries and materials, and geometries of corrugated tubes on relative velocities and drag coefficients were investigated. The present work showed that the drag force coefficients of particles in the corrugated tubes were usually lower than those in the smooth tubes, meanwhile the relative velocities between particles and water in the corrugated tubes were little higher than those in the smooth tubes except the particles of glasses.

에너제틱 금속입자 제조 및 안정화 기술 (Preparation of Energetic Metal Particles and Their Stabilization)

  • 이혜문;김경태;양상선;유지훈;김용진
    • 한국입자에어로졸학회지
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    • 제9권3호
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    • pp.173-185
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    • 2013
  • Oxidations of metal generate large quantity of thermal and light energies but no toxic pollutants, so that metals with high calorific values, such as beryllium, boron, aluminum, magnesium, and lithium, are possible to be used as clean fuels instead of fossil fuels. However, they are so explosive due to very high oxidation rates that they should be stabilized by their surface passivation with oxides, organics and inorganics. For reasonable use of energetic metal particles as solid fuel, therefore, some detail information, such as thermal properties, preparation and passivation methods, and application area, of the energetic metals is introduced in this manuscript.

극미세 구리합금입자(NICO)를 이용한 특수윤활유가 박용기관 성능에 미치는 영향 (The Effect of Lubricant Containing Copper Alloy Fine Particles on a Marine Diesel Engine)

  • 소병두;임희성;박권하
    • 한국마린엔지니어링학회:학술대회논문집
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    • 한국마린엔지니어링학회 2000년도 추계학술대회 논문집(Proceeding of the KOSME 2000 Autumn Annual Meeting)
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    • pp.61-67
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    • 2000
  • Many research works for improving a boundary lubrication performance have been executed by using solid lubricants, and been tried to apply an engine lubrication. However those general lubricants like MoS$_2$ or PTFE have not been applied on engines due to the extreme conditions such as very high temperature and pressure by combustion process in a cylinder. A copper nickel alloy fine particle has been introduced and studied. In this Paper the lubricant using the alloy Particles is applied on a marine diesel engine and assessed by the engine performance test The results showed the increase of cylinder pressure related strongly to the engine efficiency as well as the improving the engine lubrication performance.

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파형관 튜브가 있는 순환유동층 원통다관형 열교환기 내의 유체유동 (Fluid Flow in the Fluidized Bed Shell and Tube Type Heat Exchanger with Corrugated Tubes)

  • 안수환;이병창;배성택
    • 설비공학논문집
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    • 제15권5호
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    • pp.406-412
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    • 2003
  • An experimental study was carried on the characteristics of fluid flow and heat transfer in a fluidized bed shell-and-tube type heat exchanger with corrugated tubes. Seven different solid particles having same volume were circulated in the tubes. The effects of various parameters such as water flow rates, particle geometries and materials, and geometries of corrugated tubes on relative velocities and drag coefficients were investigated. The present work showed that the drag force coefficients of particles in the corrugated tubes were usually lower than those in the smooth tubes, meanwhile the relative velocities between particles and water in the corrugated tubes were little higher than those in the smooth tubes except the glass.