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Abstract
A three-dimensional particle dynamic analyzer (3D-PDA) was employed to measure the gas-solid two-phase flow in a lab-scale square cyclone
separator with downward gas-exit. Several cases of different inlet velocity and particle concentration were studied. The particle used in the test
was glass bead of mean diameter 30-40 p,m. Discussion was given on the distribution of flow vector, mean velocity, turbulent intensity and kinetic
energy of both gas and particles of different diameter at different position in the separator. It was found that the center of the flow field deviated
from the geometric center of the cyclone. The flow fields had the feature of Rankine eddy, i.e., strongly swirling region in the central part and
pseudo-free eddy region of weak swirling intensity near the cyclone wall. Local vortex existed at the corners where the flow changed its direction
sharply. When the cyclone wall was heated and the suspension temperature was elevated, the flow field became more uniform than that under
room-temperature condition. The local vortexes at the corners were weakened and the swirling intensity became poorer which led to decreased total
mean separation efficiency from about 81 % to 76.5%. The right-side wall facing the suspension inlet gave the major contribution to the separation
efficiency, where the largest downward velocity was measured. Back-flow (upward velocity) was found around the center of the separator above
the gas-exit. The quasi-laminar motion of particles enhanced the turbulent motion at the corners due to particle-particle or particle-wall collision,
which led to the local peak value of the turbulent kinetic energy and turbulent intensity. The corner was one of the major regions to cause pressure
drop and was found to be beneficial to particle separation mainly because the strong fluctuating flow consumed much of the kinetic energy of both
the particle and gas.
⑥2006 Elsevier B.V. All rights reserved.
Keywords: Square-shaped cyclone separator; Circulating fluidized bed; Turbulent flow; Three-dimensional particle dynamic analyzer (3D-PDA)
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一个三维粒子动态分析仪(3D-PDA)被用来测量气固两相流在lab-scale广场旋风
gas-exit分离器与向下。几个例子中不同的入口速度和颗粒含量进行了研究。试验中采用的粒子
是玻璃珠的平均直径30 - 40磷、米。讨论了流动矢量分布、湍流强度、平均流速、动力学
两种气体和颗粒能量在不同位置的不同直径的分隔符。研究发现,该中心的流场歪
从遭受强热带风暴袭击的几何中心。流场有软的特点,即:强烈的旋转涡流区域,在中部和
pseudo-free艾迪的地区附近的旋转强度弱强热带风暴的墙。当地的漩涡存在的角落里,改变了其方向流动
急剧下降。当飓风墙是加热和温度升高,悬浮流场条件下,变得更加均匀
室温条件。当地的涡流在嘴角都受到削弱和旋转强度较差,从而导致了降低成为总数
代表分离效率,从81左右76.5%¥。墙上悬挂右半面临进口给了重大贡献的分离
效率,
最大的地方,测量向下速度Back-flow(向上速度)被发现的中心周围的分离器以上
这gas-exit。quasi-laminar粒子的运动,增强了湍流运动的四角由于particle-particle或particle-wall碰撞,
这导致了当地的峰值湍流动能和湍流强度。角落的是其中最主要的地区造成压力
降和被发现是有益的粒子进行分离流动强烈的波动主要是由于消耗了很多的动能的共同之处
粒子和天然气。
⑥2006年农业B.V.保留所有权利。
关键词:哑铃型、循环流化床旋风分离器;;紊流三维粒子动态分析仪(3D-PDA)
2021-09-06 20:37
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本专业学生主要学习发电厂、电力系统及其自动化等方面的设计和运行的基础理论、基本知识和基本技能。毕业后授予工学学士学位。
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关雄,男,1957年10月16日生,福建莆田人,中共党员,教授,昆虫学博士,博士生导师,现任“生物农药与化学生物学”教育部重点实验室主任,学术委员会委员, 国家“新世纪百千万人才”,国际无脊椎动物病理学会会员、国际生防组织亚太地区会员、中国农业生物技术学会常务理事、微生物分会副会长、中国农学会理事、中国农业生物化学与分子生物学会常务理事,享受国务院政府特殊津贴专家。福建省第7次党代会代表;中国人民政治协商会议第十届福建省委员。
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