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气固流化床与水平埋管之间换热系数的计算 总被引:1,自引:0,他引:1
由于大颗粒床与小颗粒床在气泡行为方面的明显不同,导致它们在传热机理上的差异,本文在气固流化床与水平埋管之间换热系数的计算方面,把流化床分为大颗粒床与小颗粒床两种情况处理,并将Saxena等人关于换热系数的计算关联式与国内部分研究者的实验结果进行了比较,为气固流化床与水平埋管表面之间换热系数的计算提供了一定的依据. 相似文献
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布风板结构参数显著地影响着床层内部气固两相流流动特性,为了探究流化床干燥装置内油菜籽颗粒流化性能和空气流速脉动规律,明晰不同面板凸度、风帽开孔夹角和开口瓣数对风帽布风板布风性能的影响,提出布风板结构数的优化方案。以15.84%开孔率圆形非均匀布孔布风板为基础,根据Euler/Euler双流体模型和Standardk-ε湍流模型,采用ANSYS19.1中流体动力学分析模块Fluent软件对面板凸度(2 mm、5 mm和10 mm)、风帽开孔夹角(0°、5°和10°)和开口瓣数(四瓣、六瓣和八瓣)进行优化设计,并通过实验进行验证。结果表明:5 mm凸度球面板、四瓣风帽、5°开孔夹角布风板是油菜籽流化床干燥的最佳布风板。与平面布风板相比,凸形球面布风板的油菜籽分布均匀性好,其中凸度为5 mm球面板油菜籽平均体积分数方差(0.007 3)最小,促使其与热空气接触均匀充分。5°风帽开孔夹角有利于颗粒运动呈现脉动流动,是油菜籽干燥布风板的最佳开孔夹角。风帽开口瓣数对油菜籽流化床干燥的布风性能影响不大,相对来说四瓣风帽开口瓣数能更好地均布空气流。通过实验对模拟结果进行验证,结果发现数值模拟与实验结果... 相似文献
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流化床内颗粒聚并和破碎将影响颗粒相的流动特性.本文运用基于颗粒动理学理论的欧拉一欧拉气固多相流模型,利用直接矩积分方法求解颗粒数平衡方程,建立颗粒数密度与连续性方程、动量方程之间的关系,数值模拟流化床内两种不同直径颗粒发生聚并时气固两相流动特性。计算结果表明,颗粒聚并伴随着床内颗粒直径逐渐增大,床内颗粒流化状态逐渐变为固定床状态,两种颗粒直径均增加,且小颗粒的体积分数逐渐减小、大颗粒的体积分数增加。当仅考虑聚并过程时增加流化速度将导致床内颗粒体积平均直径变大。随着颗粒密度减小,床内体积平均直径增加。 相似文献
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Convective heat transfer coefficients were measured experimentally for a tube immersed vertically in a circulating fluidized bed. Circulating fluidized beds operate in the dilute transport regime of two-phase (solid/gas) flow. The dominant mechanism for heat transfer to surfaces is particle-induced convection. In this study, experiments were carried out in a circulating fluidized bed of15 cm diameter and 11 m height. An instrumented tube of 9.5 mm diameter and 1.3 m length was placed vertically at the centeriine of the fluidized bed to measure convective heat transfer coefficients at several different elevations in the bed. Three types of particles, with mean diameters ranging from 68 to 2S1 urn, were used in the experiments at superficial gas velocities in the range of 1.3 to 8.2 m/s. Results showed that the convective heat transfer coefficients with solid/gas two-phase circulation were two to three times greater than those for single-phase gas convection at the same velocity. For a given gas velocity, the coefficients increased with increasing solid mass flux, but decreased with elevation. It was demonstrated that the heat transfer coefficients for the immersed tube and for the bed wall could be correlated with different functional dependence on the two-phase suspension density. 相似文献
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1引言燃烧流化床声发射是一个极其复杂的过程,它是气因流态化两相流运动,气体湍动和燃烧化学反应复合作用的结果,其发射声谱中包含了上述运动过程的丰富信息山,对其发射声谱进行系统深入的研究,对寻求流态化两相流的运动规律有重要意义。本文试图以大量的实验研究为基础,以声波数字计算技术和现代分析理论手段,对气因流态化两相流运动规律进行了研究。2实验简介实验装置主要有燃煤流化床燃烧实验台和声波测量系统组成。燃煤流化床燃烧实验台如图1所示,声波测量系统见图2,从燃烧室不同位置测得的声波信号,一路送声波数字化处理… 相似文献
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