共查询到19条相似文献,搜索用时 157 毫秒
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本文以熔盐堆脱气系统中旋叶式气泡分离器为研究对象,利用数值分析软件Fluent对分离器内的流场进行了数值模拟,并分析了其工作原理和影响因素。首先,不同的湍流模型计算结果与实验现象的对比分析表明,雷诺应力模型在不同工况下计算得到的流场分布与实验现象符合最好。在确定适合用于模拟旋叶式气泡分离器内流场的计算模型基础上,对分离器内流场作进一步的计算分析。结果表明,水在流量20 m3·h-1条件下,流经分离器搅浑叶片后,会形成一种中心低速低压的旋转流动,且在横截面中心区域附近存在很大的径向压降梯度,如果水流中存在少量气泡,便会在压力梯度的作用下,流向分离器中心,汇聚形成稳定的气芯,从而实现对流体中气相的连续分离。 相似文献
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《核动力工程》2015,(5):75-79
建立基于拉格朗日-欧拉方法的气-液两相流动的数学模型,利用商用计算流体力学软件CFX对该模型求解,数值模拟几何缩比后AP1000旋叶式汽-水分离装置内部冷态工况下气-液两相流动特性。模型中空气为连续相,其内运动的液滴视作离散相,针对液滴在流场中的运动特点,考虑液滴受到曳力、虚拟质量力、浮力和重力,并以此建立空气和液滴动量双向耦合的动力学模型。针对9个不同工况,利用CFX软件对两相流模型进行求解,得到不同直径大小的液滴在流场内的运动轨迹,进而得到分离器的分离效率和进出口总压降。结果显示:分离效率的计算值与冷态实验数据非常吻合,且压降计算值与冷态实验值变化趋势基本一致,验证所建立模型的正确性。 相似文献
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基于Matlab软件开发了自动识别气液两相流界面程序,程序可获得气液界面变化、汽膜厚度、汽膜脱离周期和汽膜法向速度等特征。利用该程序对沟槽结构加热表面朝下布置时,在不同倾角、不同热流密度下的汽泡动态数据进行了处理和分析。结果表明:加热表面朝下发生核态沸腾时,汽膜厚度随热流密度的增大而增大,汽泡脱离周期随热流密度的增大先减小,而后维持在一稳定值;汽膜脱离周期随倾角的增大而减小,倾角为5°时的汽膜脱离周期稳定在0.27 s左右。当发生沸腾危机时,汽膜厚度迅速减小,这可作为动态监测加热表面沸腾状态的依据。 相似文献
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板壁水膜波动流动数值研究 总被引:1,自引:0,他引:1
板壁水膜流动特性是影响水膜二次携带的主要因素之一.通过数值方法对某一规格板壁表面水膜波动流动特性进行研究.在对水膜表面进行受力分析的基础上,得出了水膜自由表面的动力学边界条件,建立了板壁水膜波动流动的数学模型.连续性方程采用中心差分格式,动量方程采用迎风和中心差分混合的偏心差分格式,采用Simple算法对板壁水膜波动流动方程进行了求解,采用流体界面追踪法(VOF:Volume-of-Fluid)方法对水膜自由表面进行模拟追踪.计算结果表明,水膜在板壁中部的波动比其它部位剧烈,另外也发现入口扰动频率对水膜波动的影响程度要大于扰动振幅对水膜波动的影响. 相似文献
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棒束通道中环状流气液界面行为的研究,能为压水堆的事故处理和沸水堆电厂的正常运行提供数据和理论支撑。本研究针对3×3棒束通道中环状流气液波状界面形式进行记录与分析,绘制详细的环状流流型图,并针对其形成机理进行分析。结果表明:棒束通道中的环状流主要有搅混型、未全润湿、平滑边界型、单一波状流、包状扰动波、带状扰动波和带状扰动波叠加液相丧失7种形式;单一波状流是当气相速度较高、液相速度较低时,气液界面上发生的有固定波峰和波谷、以固定速度向上运动的流动形式,其现象可通过Kelvin-Helmholtz型不稳定性理论来解释;当液相流量升高或气相流量减少时,发生单一波状流界面失稳,界面能量增加,进入到包状扰动波或带状扰动波阶段;当能量超过1.6 kPa2/Hz时,界面能量超过底层液膜束缚能力,产生液相丧失型环状流。 相似文献
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Masanori Aritomi Akira Inoue Shigebumi Aoki Keiji Hanawa 《Nuclear Engineering and Design》1990,120(2-3):281-291
The thermo-hydraulic behavior of inverted annular flow was investigated experimentally under various heat flux, inlet velocity, inlet subcooling and heating length conditions using freon 113. Empirical correlations are proposed concerning the net vaporization rate from the interface, heat flux from the interface to the liquid phase, interfacial shear stress and heat transfer coefficient from the wall to fluid. It is found that the roughness of the interface between the vapor film and liquid jet increases with the thickness of the vapor film and that an increase in the vapor film thickness causes the average Nusselt number and interfacial friction factor to rise linearly. On the other hand, the wall shear stress in inverted annular flow is lower than that in liquid single-phase flow due to the existence of a vapor film at the wall. 相似文献
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An experimental study was conducted to investigate the effect of non-condensable gas and wavy water film on condensation heat transfer. The experiment was performed in a nearly horizontal (4.1°) square duct of 0.1 m height, 0.15 m width and 1.52 m length at atmospheric pressure. A water film in a steady thermal condition was injected to simulate the effect of a wavy interface on the condensation. The experimental data for the heat transfer coefficient and the interfacial structure of the wavy condensate were obtained along with the three parameters: air mass fraction, mixture velocity and film flow rate. When the interface is smooth, the heat transfer coefficients with or without non-condensable gas agree reasonably with the previous theories. The waviness of condensate film increases the heat transfer up to several tenths of a per cent. 相似文献
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Youjia Zhang Guanghui Su Suizheng Qiu Wenxi Tian Hua Li Libo Qian Yong Li Xiao Yan Yanping Huang 《Nuclear Engineering and Design》2011,241(12):4704-4713
Two-phase flow instability and dynamics of a parallel multichannels system has been theoretically studied under periodic excitation induced by rolling motion in the present research. Based on the homogeneous flow model considering the rolling motion, the parallel multichannels model and system control equations are established by using the control volume integrating method. Gear method is used to solve the system control equations. The influences of the inlet, upward sections, heating power and rolling amplitudes on the flow instability under rolling motion have been analyzed. The marginal stability boundary (MSB) under the rolling motion condition is obtained. The unstable regions occur in both low and high equilibrium quality and inlet subcooling regions. The multiplied period phenomenon occurs in the high equilibrium quality region and the chaos phenomenon appears on the right of MSB. The concept of stability space is presented. 相似文献
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Tetsuhiro Ozaki Takashi Hibiki Shuichiro Miwa Michitsugu Mori 《Journal of Nuclear Science and Technology》2018,55(8):911-930
In gas–liquid two-phase flow simulation for reactor safety analysis, interfacial momentum transfer in two-fluid model plays an important role in predicting void fraction. Depending on flow conditions, a shape of the two-phase interface complicatedly evolves. One of the proposed approaches is to quantify the gas–liquid interface information using interfacial area transport equation. On the other hand, a more simplified and robust approach is to classify bubbles into two-groups based on their transport characteristics and utilize constitutive equations for interfacial area concentration for each group. In this paper, interfacial drag model based on the two-group interfacial area concentration correlations is implemented into system analysis code, and void fractions were calculated for the evaluation of numerical behaviors. The present analysis includes (1) comparison of one-group and two-group relative velocity models, (2) comparison with separate effect test database, (3) uncertainty evaluation of drag coefficient, (4) numerical stability assessment in flow regime transition, and (5) transient analysis for simulating the prototypic condition. Results showed that utilization of interfacial drag force term using constitutive equations of two-group interfacial area concentration yields satisfactory void fraction calculation results. The proposed solution technique is practical and advantageous in view of reducing the computational cost and simplifying the solution scheme. 相似文献