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    Please use this identifier to cite or link to this item: http://ir.lib.ncu.edu.tw/handle/987654321/65955

    Title: 應用於生質物快速熱裂解之氣泡流體化床反應器其熱傳遞現象之模擬分析研究;CFD modeling of hydrodynamics with heat transfer in bubbling fluidized-bed reactors applied to fast pyrolysis of biomass
    Authors: 丁公平;Dinh,Cong-binh
    Contributors: 機械工程學系
    Keywords: 生質物快速熱裂解;流體化床反應器;流體動力學;計算流體力學;固體混合;尤拉多重流體模型;biomass fast pyrolysis;fluidized bed reactor;hydrodynamics;computational fluid dynamics;solids mixing;Eulerian multifluid model
    Date: 2014-07-25
    Issue Date: 2014-10-15 17:19:08 (UTC+8)
    Publisher: 國立中央大學
    Abstract: 本研究探討在生物質快速熱裂解過程中發生的流體力學和熱傳遞現象。透過結合尤拉多重流體模型和顆粒流的動力學理論之數值方法並將其應用到模擬氣泡流化床反應器的氣-固流動行為。在這項研究中,具有特定屬性的稻殼和石英砂在此分別作為生物質和熱惰性物質。由於這些系統的動態特性往往是混亂的,故該模型首先以先前的研究結果加以驗證其可行性,接下來就參數方面進行一廣泛的研究,以確定其對流動分佈和相位之間的熱傳遞的主要變量的影響。該組統御及組成方程式是由商業計算流體力學程式軟體,ANSYS FLUENT 13.0.0解得。在此,各個方面,如固相體積分率,速度,床體混合,粒子溫度,熱溫度,壓力,排除輻射熱傳遞機制也進行了詳細研究。從兩個不同的拖曳模式,即,Syamlal-O′Brien和Gidaspow結果的比較,也包涵在本論文中。結果發現,不同拖曳模型和預測壓降之間沒有顯著差異,而隨著增加的進氣速度而稍微的增加。壓降則隨著生物質初始體積分率的的減少而增加。
    ;The present study investigates the hydrodynamics and heat transfer phenomena that occur during the biomass fast pyrolysis process. A numerical approach that combines an Eulerian multifluid model and the kinetic theory of granular flow applied to simulate the gas-solid flow in a bubbling fluidized bed reactor. In this study, rice husk and quartz with specified properties have been used as biomass and inert material, respectively. Since the dynamics of these systems are often chaotic, the model was first validated the feasibility using previous findings, then an extensive parametric study was conducted to determine the effects of the major variables on the flow distribution and the heat transfer between the phases. The set of governing and constitutive equations was solved by the commercial computational fluid dynamics code, ANSYS FLUENT 13.0.0. Herein, various aspects such as solid volume fraction, velocities, bed mixing, granular temperature, thermal temperature, pressure, heat transfer mechanisms excluding radiation were studied in detail. A comparison of results from two different drag models, namely, Syamlal-O’Brien and Gidaspow, was also included in this thesis.
    It was found that there was no significant difference between the predicted pressure drops for different drag models, whereas it slightly increased with the increasing inlet gas velocity. The pressure drop increased with decreasing the initial volume fraction of biomass.
    The distribution of solid volume fraction and velocity profiles were obtained for different cases. Although the results revealed the inherently chaotic nature of fluidized bed, the general trends were still obtained which agree good with previous studies.
    The results also indicated that the solids mixing was strongly influenced by the inlet gas velocity and the initial volume fraction of biomass. Better particle mixing could be obtained by increasing the inlet gas velocity.
    The granular temperatures of both solids were found to be higher near the bottom and the top portion of the bed. It increased with the increasing inlet gas velocity but with the decreasing initial percentage of biomass.
    The heat transfer happening inside the fluidized bed was described by the distribution of solids temperature, the variation of heat transfer coefficients and the surface heat fluxes. Both heat transfer quantities were observed to be dominant in the dense bed regions as they strongly depend on the solids concentration in the fluidized bed. Due to the strong mixing, the distribution of biomass temperature was fairly homogeneous in the bed region. The increasing inlet gas velocity promoted the mixing of solid particles, thus resulted in effective heat transfer between the particles and wall to particles. There was no significant difference between the simulated total surface heat fluxes for different drag models.
    Overall, the current results were based on some assumptions and in two-dimensions only due to the limit of time and computational effort during this work. Therefore, those results could not describe the adequately thermo-physical processes occurring in the fluidized bed reactor. A full three-dimensions model with less assumptions should be taken into account in future work. Furthermore, a quantitative comparison of the simulations with the experimental results can be done to further validate the utility of the suggested setup.
    Appears in Collections:[機械工程研究所] 博碩士論文

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