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PIV对射流煤粉火焰流场特性的分析 总被引:1,自引:0,他引:1
《工程热物理学报》2015,(6)
为研究湍流煤粉射流进入高温环境后的流动及混合特性,采用PIV测量平流射流煤粉燃烧器中心射流区域的流场特性。通过对不同示踪粒子特性的分析,选定SiC表征气相流场,选定煤粉表征煤粉射流流场。实验结果表明;煤粉具有较好的散射特性,因而采用PIV可获得合理的煤粉颗粒流场;相同射流速度下,冷态射流比热态有更强的湍流脉动特征,主要原因是热态条件下气流黏度增加2~3倍,显著降低射流Re。 相似文献
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炉内两相流动和煤粉燃烧的双流体-轨道模型 总被引:9,自引:0,他引:9
本文首次用双流体一轨道(连续介质-轨道CT)模型对大尺寸四角喷燃炉内气粒两相流动及煤粉燃烧进行了模拟。该模型基于欧拉气相方程组、欧拉颗粒连续方程和动量方程以及拉氏颗粒能量和质量变化的方程,对各子模型用k-ε-kp两相湍流模型,EBU-Arrhenius湍流燃烧模型,煤粉颗粒的水分蒸发,热解挥发和焦炭燃烧的扩散-动力模型,DO(离散坐标)辐射模型。采用了将坐标扭转一定角度的方法减小入口射流和网格斜交造成的伪扩散。编制了LEAGAP-FURNACE-3程序,分别对冷态模型炉内两相流动和大尺寸炉内三维两相流动和煤粉燃烧进行了模拟,并与颗粒轨道(ST)模型的模拟结果进行了对照。采用PDPA对冷态模型炉内气粒两相流场进行了测量。冷态两相流动的模拟与实验结果的对比表明CT模型的模拟结果和实验符合较好,ST模型所得颗粒浓度分布和实验山入较大。热态模拟的结果给出了两相速度,气相温度,组分浓度和壁面热流分布。模拟结果定性合理。模拟结果显示在出口处由于气流旋转,有一局部高温区存在。 相似文献
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使用RKE模型和RSM模型对某旋流燃烧器进行3D冷态湍流流动模拟计算,并从精度、计算量和收敛性3个方面对两个模型进行了比较。通过与PIV所测得的出口冷态流场对比表明,两个模型均可以较准确地预测燃烧器出口的宏观流场、径向速度和轴向速度分布。相比较而言,RSM模型在预报流场速度峰值的位置、回流区的大小、主流射流宽度等方面比RKE模型更准确一些,在收敛性上RSM模型也占优,而在计算量上,RSM模型略大一些,但对反应流计算,两个模型计算量基本一致。研究表明在模拟旋流燃烧器流场时RSM模型具有一定的优越性,建议优先考虑。 相似文献
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二维槽道湍流拟序结构的大涡模拟 总被引:2,自引:0,他引:2
本文采用大涡模拟的方法,对二维槽道湍流流动进行了数值模拟。采用Chorin的分步投影法求解大尺度涡运动的Navier-Stokes方程,小尺度涡采用三种亚格子(SGS)模式分别模拟,给出了不同亚格子涡粘性模式下的模拟结果。对固壁面采用了壁函数。模拟结果再现了二维槽道流动拟序结构的发展演变过程。通过对不同入口速度下的瞬态流场的比较,揭示了入口速度分布对流场的影响。 相似文献
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本文应用强旋湍流气一固两相流动和煤粉燃烧的数学模型,对新型涡旋燃烧炉内的流动、传热和燃烧过程进行了系统的模拟和分析,得到了与实验相符合的结果。结果表明,涡旋燃烧炉内的湍流空气动力场分布具有强旋、回流和正在发展流的特点。水冷壁总吸热量随燃烧热负荷的增大成比例地增加。煤粉颗粒在炉内的平均停留时间随初始粒径的增大而加长。炉内可实现煤粉的低温、强旋、高效率和高强度燃烧。 相似文献
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A turbulent velocity model is proposed to describe certain types of turbulent flows. An expression of the photon correlation function for laser cross-beam light scattering based on this model is presented, and it is found to give excellent agreement with experimental data. With least-square fitting, the measured spectrum allows the simultaneous determination of the mean flow velocity, turbulent velocity, and the number of scatterers. 相似文献
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Experiments were conducted to investigate the flow characteristics of water flowing through rectangular microchannels having hydraulic diameters of 0.133-0.367 mm and H/W ratios of 0.333-1. Experimental results indicated that the laminar flow transition occurred at Reynolds numbers of 200-700. This critical Re for the laminar transition was strongly affected by the hydraulic diameter, decreasing with corresponding decreases in the microchannel. In addition, the size of the transition range was diminished and fully developed turbulent flow also occurred at much lower Re. The friction behavior of both the laminar and turbulent flow was found to depart from the classical thermqfluid correlations. lite friction factor, f, was found to be proportional to Re?1.98 rather than Re for the laminar condition, and proportional to Re?1.72i for turbulent flow. The geometric parameters, hydraulic diameter, and H/W were found to be the most important parameters and had a critical effect on the flow. Generally, increasing the ratio H/W increases the friction factor. The reduction of the microchannel hydraulic radius decreases the friction factor significantly for a given H/W. There exists a special range of ratio H/W (approximately 0.5 mm) at which the experimental data are lower than the predictions obtained from classical correlations. Continued reduction of channel size increases the difference between fI,expf1,theo at REcri, and the quantity of fI,exp becomes smaller within the region adjacent to H/W = 0.5, and larger when H /Wis out of this region. 相似文献
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