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NUMERICAL INVESTIGATION ON TWO-PHASE FLOW CHARACTERISTIC IN THE SEPARATED STRUCTURE SHELL-AND-TUBE WASTE HEAT BOILER

机译:分离结构壳管废热锅炉两相流动特性的数值研究

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The shell-and-tube waste heat boiler is a common facility to recover and utilize the energy of flue gas in industries. To improve the ability and efficiency of the boiler, a steam dome is configured above the drum so as to arrange more heat exchange tubes. Simulation and analysis of vapor-liquid two-phase flow across tube bundles arranged in the drum are of vital importance to design and safety operation. Numerical simulation of boiling two-phase flow across tube bundles in the drum was carried out to analyze the shell side thermal-hydraulics. Commercial software ANSYS FLUENT 14.5 was adopted for modeling and computational calculations. The applied modeling approach was validated against experimental results with a good agreement. In order to analyze the vapor-liquid two-phase flow performance under various working conditions, the inlet velocity of downcomer tubes of 3m·s~(-1), 4m·s~(-1) as well 5m·s~(-1) for saturated water were simulated, respectively. The pressure field, flow characteristic, void fraction distribution and heat transfer characteristic were analyzed to have a good knowledge of the boiler operation. The following conclusions have been drawn through analyzing simulation results. (1)The total pressure drop on shell side increased with increasing the inlet velocity of downcomer tubes of saturated water. (2)The velocity of saturated water decreased after flowing into the drum less than z=0.1m as the flow area increasing, and then increased rapidly as the volume of the mixture two-phase flow increasing. (3)The integral average void fraction of the drum decreased as the mass flow rate of inlet saturated water increasing. (4)The HTC (heat transfer coefficient) of the heat exchange tubes varied with the flow direction, which is related to the vapor-water void fraction. The conclusions obtained above can be used as a reference for the design of the separated structure shell-and-tube waste heat recovery boiler.
机译:壳管废热锅炉是恢复和利用行业烟气能量的常用设施。为了提高锅炉的能力和效率,在滚筒上方构造蒸汽圆顶,以便布置更多的热交换管。滚筒中排列管束的蒸汽两相流的仿真和分析对于设计和安全操作至关重要。进行了滚筒管束沸腾两相流的数值模拟,以分析壳体侧热液压。采用商业软件ANSYS流利的14.5用于建模和计算计算。应用建模方法验证了符合良好一致性的实验结果。为了在各种工作条件下分析汽液两相流动性能,下降管的入口速度为3m·s〜(-1),4m·s〜(-1),也为5m·s〜( - 1)分别模拟饱和水。分析压力场,流动特性,空隙分量分布和传热特性以具有良好的锅炉操作知识。通过分析模拟结果来绘制以下结论。 (1)随着饱和水的降液管的入口速度增加,壳体侧的总压降增加。 (2)在流入小于Z = 0.1M的滚筒时,饱和水的速度降低,因为流量面积增加,随后随着混合物的体积增加两相流的增加而迅速增加。 (3)当入口饱和水的质量流速增加时,滚筒的整体平均空隙率降低。 (4)热交换管的HTC(传热系数)随着流动方向而变化,其与蒸汽 - 水空隙级分有关。上面得到的结论可用作分离结构壳 - 管废热回收锅炉设计的参考。

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