化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
7期
2724-2732
,共9页
流化床%多相流%计算流体力学%离散元方法%小波分析
流化床%多相流%計算流體力學%離散元方法%小波分析
류화상%다상류%계산류체역학%리산원방법%소파분석
fluidized-bed%multiphase flow%computational fluid dynamics%discrete element method%wavelet analysis
采用计算流体力学和离散元方法(CFD-DEM)对气固鼓泡床流动行为进行模拟研究,并基于模拟结果分析鼓泡床内气泡和颗粒微观运动特性。对颗粒速度的脉动能谱进行分析,发现鼓泡床流场中存在间歇性。通过对比鼓泡床不同轴、径向位置的颗粒脉动速度的平坦因子,发现鼓泡床内不同位置的流场间歇性不同,随着床层高度的增加,流场的间歇性减弱;在径向上,过渡区的流场间歇性明显大于边壁区和中心区。进一步采用连续小波分析方法揭示了相干结构(颗粒涡团)的分布以及演化过程,并分析了不同尺度下相干结构(颗粒涡团)的分布与鼓泡床内颗粒与气泡运动的关系。
採用計算流體力學和離散元方法(CFD-DEM)對氣固鼓泡床流動行為進行模擬研究,併基于模擬結果分析鼓泡床內氣泡和顆粒微觀運動特性。對顆粒速度的脈動能譜進行分析,髮現鼓泡床流場中存在間歇性。通過對比鼓泡床不同軸、徑嚮位置的顆粒脈動速度的平坦因子,髮現鼓泡床內不同位置的流場間歇性不同,隨著床層高度的增加,流場的間歇性減弱;在徑嚮上,過渡區的流場間歇性明顯大于邊壁區和中心區。進一步採用連續小波分析方法揭示瞭相榦結構(顆粒渦糰)的分佈以及縯化過程,併分析瞭不同呎度下相榦結構(顆粒渦糰)的分佈與鼓泡床內顆粒與氣泡運動的關繫。
채용계산류체역학화리산원방법(CFD-DEM)대기고고포상류동행위진행모의연구,병기우모의결과분석고포상내기포화과립미관운동특성。대과립속도적맥동능보진행분석,발현고포상류장중존재간헐성。통과대비고포상불동축、경향위치적과립맥동속도적평탄인자,발현고포상내불동위치적류장간헐성불동,수착상층고도적증가,류장적간헐성감약;재경향상,과도구적류장간헐성명현대우변벽구화중심구。진일보채용련속소파분석방법게시료상간결구(과립와단)적분포이급연화과정,병분석료불동척도하상간결구(과립와단)적분포여고포상내과립여기포운동적관계。
The gas-solids flow in a bubbling bed was simulated by the combination approach of computational fluid dynamics (CFD) and discrete element method (DEM), and the simulation results were used to investigate the microscopic characteristics of bubbles and particles. The particle fluctuating energy spectrum was calculated to find out the flow field intermittency in the bubbling bed. Different features of flow field intermittency were found at different locations of bubbling bed by comparing the flatness factor of fluctuation velocity of particles. With increasing bed height, flow field intermittency was weakened. Along the radial direction, the flow field intermittency in the transition region was stronger than that in the wall and center region. Continuous wavelet transform was used to investigate the coherent structure of particles and its evolution process, as well as the relation between coherent structure of particles and flow behavior of bubbles and particles on different scales.