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流化床反应器的应用较为广泛,但是由于流化床内气泡的存在会对反应器内的传质效果带来不利影响,本文简述的提高流化气速使流化床操作向快速流态化发展以及在流化床内部添加内构件的方法,都是通过抑制或消除气泡等方法来强化气固间的接触从而达到提高气固传质效率的目的。 相似文献
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循环流态化:(Ⅱ)气—固流动规律 总被引:4,自引:0,他引:4
循环流态化气、固两相流动行为是比较复杂的,它不仅取决于气体速度、颗粒循环速率以及气、固物性;而且受设备条件(床层直径、床层高度、进、出口结构、内部构件等),操作温度和压力等因素的影响。循环流态化气、固流动的基本特征,表现在局部结构上是存在颗粒的聚集现象,表现在整体结构上为存在颗粒浓度、气体、固体运动速度等的轴、径向不均匀分布。这种局部和整体宏观上的不均匀性,相互影响,相互关联,是表征循环流态化气、固两相流动行为的重要因素,也是研究和改善循环流化床反应器的基本课题。 相似文献
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根据气、固两相流动的基本特征,循环流态化气、固两相流动模型可分为局部流动结构模型及整体流动结构模型两类。局部流动结构模型主要描述床内稀相及絮状物相的局部分布及变化,而整体流动结构模型主要描述床中空隙率。颗粒速度以及气体速度轴、径向分布及变化,其中根据实用层次不同,整体流动结构模型可分为一维、一维两区及两维模型。本文对循环流态化气、固流动模型进行了分类评述,供循环流化床反应器设计时参考。 相似文献
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气固鼓泡床是一个流动、传热/传质和反应多尺度时空耦合的复杂系统。其中介尺度流动结构(如气泡)对于气固相间传递起着关键性的作用。为了准确描述气固流态化系统中的“三传一反”行为,需要在合理物理简化的基础上建立介尺度模型。提出了基于气泡结构的多流体反应模型,考虑了介尺度非均匀结构对于鼓泡床内气固相间反应的影响;定义了基于气泡的反应非均匀因子修正双流体(TFM)传质反应模型,从而使模型更加易用。通过鼓泡床内的臭氧催化分解反应模拟,对模型进行了初步验证,模拟结果与文献结果相符。 相似文献
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The flow behavior of the bubble in gas/solid fluidized bed is studied in multi-scales.A hypotheses of taking dispersed bubble as the continuous medium and the hydromechanics expression based on volume flux are proposed.The mathematical model of radial porosity distribution in the dense zone is developed.The radial distribution of the porosity is parabolic in nature according to the theoretical calculation and the calculated data is consistent with experimental data satisfactorily. 相似文献
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I.U. Bhuiyan Author Vitae J. Mouzon Author Vitae Author Vitae J. Hedlund Author Vitae 《Powder Technology》2011,214(3):306-312
Scanning electron microscopy and image analysis was used for quantitative analysis of bubble cavities in iron ore green pellets. Two types of pellets prepared with and without addition of flotation reagent prior to balling were studied. The bubble cavity porosity amounted to 2.8% in the pellets prepared without addition of flotation reagent prior to balling. When flotation reagent was added prior to balling, the bubble cavity porosity increased by a factor of 2.4 and the median bubble diameter was decreased slightly. It was also shown that mercury intrusion porosimetry is not suitable for determination of the distribution of bubble cavities. Finally, our data suggested that the difference in total porosity determined by mercury intrusion porosimetry and pycnometry between the two types of pellets was due to the bubble cavities. 相似文献
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The point properties of bubbling systems have been calculated for various assumed bubble frequency and size distributions. Flat, linear and parabolic radial frequency distributions were considered for both uniform and non-uniform bubble size distributions.The point bubble frequency distribution, which is equivalent to the distribution measured by a probe inserted into the system, may not be representative of the distribution which actually exists in the bed. Due to a boundary effect, the theoretical probe output for larger bubbles is found to yield a peak in the bubble frequency toward the bed centre, even if the actual distribution is flat, the magnitude of the bias increasing as bubble size increases. Caution in using radial frequency profiles obtained by point probe methods is thus indicated. 相似文献
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Gary E. Mueller 《Powder Technology》2010,203(3):626-8248
A functional approach has been developed to investigate the radial porosity of mono-sized spheres in cylinders. Analytical and semi-analytical equations have been developed to calculate the local radial porosity and the radial porosity distribution, respectively, within a cylindrical packing structure. The analytical equations are based upon fundamental principles and are simple, straightforward and provide highly accurate results for the radial porosity with minimal computational prerequisites. The analytical equations have been developed for the fixed packing of identical spheres in cylindrical containers with D/d ≥ 2.0. The predicted results for the local radial porosity and the radial porosity distributions are benchmarked with an existing analytical equation and available experimental data, respectively, for mono-sized spheres in cylindrical containers. 相似文献
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采用光纤探针法和高速摄影法对垂直上升气液两相弹状流的液弹区含气率分布进行了试验研究,测试管径为15 mm。一种基于机器学习的图像处理技术用来识别气液两相界面,通过搭建气泡边界提取的神经网路系统,使用构建的气泡边界数据库对模型进行多次迭代训练,该方法可以有效地识别多种复杂类型的气泡边界。试验得到了弹状流液弹区的径向含气率分布曲线,结果表明,壁峰分布是液弹区含气率分布的主要形式,其中泰勒气泡的尾迹效应对分布形式有重要影响,尾迹的旋涡中心和含气率分布的峰值相对应。针对弹状流液弹区径向含气率分布的两个主要特征——中心局部含气率和壁峰位置,分别提出了相应的预测公式,且与本文的试验数据吻合良好。 相似文献
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三相循环流化床中气泡上升速度的实验研究 总被引:5,自引:1,他引:4
开发了一种新型的光纤探头多相流气泡测试系统,可用于气-液两相和气-液-固三相体系中气泡参数的测定。应用此系统研究了三相循环流环化床中不同径同位置气泡的上升速度分布,气泡上升速度均值的径向布以及操作条件对这现任中分布的影响。 相似文献
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带阻尼内构件鼓泡塔的研究(Ⅰ)——内构件对流速分布的影响 总被引:3,自引:2,他引:1
针对大型鼓泡塔径向流速分布不均易导致中心区域气体短路的问题,提出了在中心区域布置阻尼内构件改善流速分布的方案。冷模实验表明,阻尼内构件的加入可以有效地改善中心区域气-液流速分布,阻尼内构件尺寸对流速分布有显著影响。引入了阻力密度函数来表征阻尼内构件的影响,采用拟均相流动模型模拟含阻尼内构件的塔内流速分布,计算结果与实验测量值大体相符。 相似文献
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Bubble behavior, including bubble Sauter diameter, bubble rise velocity, bubble frequency and local gas holdup in different radial and axial positions, was measured using a dual electro-conductivity probe in air-water-glass beads fluidization systems. It has been found that the bubble characteristics differ significantly in various flow regimes, depending on the operating conditions; the radial distribution of bubble parameters also changes from one flow regime to another. Thus, it is necessary to employ local bubble behavior in the modeling of three-phase fluidized beds. 相似文献