• 제목/요약/키워드: Fluid-bed

검색결과 219건 처리시간 0.023초

원추형 유동층 연소기 내의 열전달에 미치는 복원계수의 영향에 대한 수치해석 연구 (A Numerical Study on the Effect of Coefficient of Restitution to Heat Transfer in a Conical Fluidized Bed Combustor)

  • 강승모;박외철;;고동국;임익태
    • 반도체디스플레이기술학회지
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    • 제14권4호
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    • pp.38-44
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    • 2015
  • In this paper, numerical simulations on conical fluidized bed combustors were carried out to estimate the effect of coefficients of restitution between particle and particle and particle to wall on hydrodynamics and heat transfer. The Eulerian-Eulerian two-fluid model was used to simulate the hydrodynamics and heat transfer in a conical fluidized bed combustor. The solid phase properties were calculated by applying the kinetic theory of granular flow. Simulations results show that increasing the restitution coefficient between the particle and particle results in increasing the bed pressure drop. On other hand, the increasing of particle to wall coefficient of restitution results in decreasing the bed pressure drop. It is found that the coefficient of restitution has little effect on heat transfer.

Characterization of flow properties of pharmaceutical pellets in draft tube conical spout-fluid beds

  • Foroughi-Dahr, Mohammad;Sotudeh-Gharebagh, Rahmat;Mostoufi, Navid
    • Journal of Industrial and Engineering Chemistry
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    • 제68권
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    • pp.274-281
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    • 2018
  • Experimental studies of the hydrodynamic performance of the draft tube conical spout-fluid bed (DCSF) were conducted using pharmaceutical pellets. The experiments were carried out in a DCSF consisted of two sections: (a) a conical section with the cross section of $120mm{\times}250mm$ and the height of 270 mm, (b) a cylindrical section with the diameter of 250 mm and the height of 600 mm. The flow characteristics of solids were investigated with a high speed camera and a pezoresistive absolute pressure transducer simultaneously. These characteristics revealed different flow regimes in the DCSF: packed bed at low gas velocities, fluidized bed in draft tube at higher gas velocities until minimum spouting, and spouted bed. The stable spouting was identified by the presence of two dominant frequencies of the power spectrum density of pressure fluctuation signature: (i) the frequency band 6-9 Hz and (ii) the frequency band 12-15 Hz. The pressure drops across the draft tube as well as the annulus measured in order to better recognize the flow structure in the DCSF. It was observed that the pressure drop across the draft tube, the pressure drop across the annulus, and the minimum spouting velocity increase with the increase in the height of draft tube and distance of the entrainment zone, but with the decrease in the distributor hole pitch. Finally, this study provided novel insight into the hydrodynamic of DCSF, particularly minimum spouting and stable spouting in the DCSF which contains valuable information for process design and scale-up of spouted bed equipment.

폐기물 층 연소와 노내 유동 해석 (Combined Bed Combustion and Gas Flow Simulation for a Grate Type Incinerator)

  • 류창국;신동훈;최상민
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2000년도 제20회 KOSCO SYMPOSIUM 논문집
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    • pp.67-75
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    • 2000
  • Computational fluid dynamics(CFD) analysis of the thermal flow in a municipal solid waste(MSW) incinerator combustion chamber provides crucial insight on the incinerator performance. However, the combustion of the waste bed is typically treated as an arbitrarily selected profile of combustion gas. A strategy for simultaneous simulation of the waste bed combustion and the thermal flow fields in the furnace chamber was introduced to substitute the simple inlet condition. A waste bed combustion model was constructed to predict the progress of combustion in the bed and corresponding generation of the gas phase species, which assumes the moving bed as a packed bed of homogeneous fuel particles. When coupled with CFD, it provides boundary conditions such as gas temperature and species distribution over the grate, and receives radiative heat flux from CFD. The combined simulation successfully predicted the physical processes of the waste bed combustion and its interaction with the flow fields for various design and operating parameters, which was limited in the previous CFD simulations.

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PROPAGATION OF SURFACE WAVES ON IRREGULAR BED TOPOGRAPHY

  • WARKE A. S.;DAS S. K.;DEBNATH L.
    • Journal of applied mathematics & informatics
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    • 제20권1_2호
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    • pp.197-208
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    • 2006
  • This paper deals with the exact solution of surface gravity waves in an ocean with irregular bed topography. In order to obtain water surface elevation and run-up of infra-gravity waves when the bed is either wavy or exponential, closed form solutions are obtained. Numerical computations indicate that when solitary wave or sinusoidal wave conditions are applied at the boundary, water surface elevation attains near Gaussian profile.

원추형 유동층 연소기의 수력학적 특성 및 열전달에 항력 모델이 미치는 영향에 대한 연구 (Effects of Drag Models on the Hydrodynamics and Heat Transfer in a Conical Fluidized Bed Combustor)

  • 강승모;;고동국;박외철;임익태
    • 대한기계학회논문집B
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    • 제39권11호
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    • pp.861-869
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    • 2015
  • 본 연구에서는 서로 다른 항력 모델이 원추형 유동층 연소기 내의 수력학적 특성과 열전달 현상에 미치는 영향에 대해, 입자상 유동에 대한 분자운동론을 적용한 오일러-오일러 모델을 사용하여 수치 해석적으로 연구하였다. Gidaspow 항력 모델과 Syamlal-O'Brien 항력 모델에 대해 유입 공기의 속도와 입자의 크기를 변화시키면서 연소기 내의 압력강하나 베드 팽창률 및 벽과 베드 사이의 열전달 계수의 변화를 조사하였다. 그 결과 베드의 팽창률은 속도가 증가함에 따라 커졌으며 압력강하는 속도의 증가에 따라 감소하였다. 벽과 베드 사이의 열전달 계수는 유입 속도가 증가하면 증가하고 입자의 크기가 증가하면 감소하는 것으로 나타났다. 베드의 팽창률이나 압력 강하와 같은 수력학적 특성은 항력 모델에 큰 영향을 받지 않았으나 열전달 계수는 항력 모델에 따라 차이가 나타났다.

자갈축열층의 공기유동 및 축열성능 (The Fluid Flow and Heat Storage Performance in Thermal Storage Bed using Gravel)

  • 이종원
    • 한국농공학회논문집
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    • 제56권3호
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    • pp.75-81
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    • 2014
  • Fossil energy is needed for a whole year greenhouse cropping due to climate in South Korea. Because the most of the fossil energy resources is imported, it is necessary to develop technology to be able to reduce the energy cost in order to manage greenhouse profitably. The greenhouse commonly consume less amount of energy as compared to other industrial sectors. Replacement of fossil fuel with solar thermal storage, therefore, can be an economical as well as environmentally sustainable option for greenhouse heating. The fluid flow, heat storage and radiation characteristic of the gravel bed model were analyzed to provide basic data for design of the experimental solar heated greenhouse with underground thermal storage using gravel. The air flow velocity in the gravel storage bed was proven to be affected from the capacity of circulation fan and the circulation method and the positive pressure method was proven to be the best among the different air circulation methods. The initial air temperature of the thermal storage bed of 1.2 m $wide{\times}9$ m $long{\times}0.9$ m deep was $10^{\circ}C$. After the thermal storage bed is heated by air of the mean temperature $4^{\circ}C$ during 9 hours, the temperature has increased about $20.3^{\circ}C$ and the storage of heat was about 33,000 kcal. The important factors should be taken into consideration for design of the solar heated greenhouse with underground thermal storage using gravel are insulation of rock storage, amount of storing heat, inflow rate and direction of inlet and outlet duct.

다공성 매질 접근법을 적용한 하이브리드 로켓 N2O 촉매 점화기의 열적 현상 (Thermal Phenomena of an N2O Catalyst Bed for Hybrid Rockets Using a Porous Medium Approach)

  • 유우준;김수종;김진곤;장석필
    • 한국항공우주학회지
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    • 제34권9호
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    • pp.89-96
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    • 2006
  • 본 연구에서는 소형 위성용 하이브리드 로켓 점화장치에 적용되는 N2O 촉매 베드의 유동 및 열적 현상에 대한 이론적인 고찰을 하였다. 허니콤 형상을 가지는 촉매 베드 내의 열적 현상을 분석하기 위해서 다공성 매질 접근법을 사용하였다. 유동장은 Brinkman- extended Darcy 모델을 사용하였고, 온도장은 One-equation 모델을 사용하여 촉매 베드 내에서 유동장 및 온도장에 대한 해석해들을 구하였다. 다공성 매질 접근법을 적용한 모델의 해석해와 기존 실험결과를 비교하여 본 모델의 정확성을 검증하였다. 해석해에 근거하여 N2O 촉매 베드에 영향을 미치는 중요한 변수들이 촉매 베드의 기공률, 유효 체적비, 촉매 베드와 기공의 직경비, 공급열, 그리고 펌핑파워임을 확인하였으며 촉매 베드 내에서의 열적현상에 대한 중요 변수들의 효과를 연구하였다.

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.

순환유동층 열교환기내 유동과 열전달 특성 (Characteristics of Fluid Flow and Heat Transfer in a Fluidized Bed Heat Exchanger)

  • 안수환;이병창;김원철;이윤표
    • 설비공학논문집
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    • 제14권4호
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    • pp.315-323
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    • 2002
  • The commercial viability of heat exchanger is mainly dependent on their long-term fouling characteristics because the fouling increases the pressure loss and degrades the thermal performance of a heat exchanger. An experimental study was performed to investigate the characteristics of fluid flow and heat transfer in a fluidized bed heat exchanger with circulating various solid particles. The present work showed that the drag force coefficients of particles in the internal flow were higher than those in the external flow, in addition, the solid particle periodically hitting the tube wall broke the thermal boundary layer, and increased the rate of heat transfer. Particularly when the flow velocity was low, the effect was more pronounced.

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.