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机构地区:[1]山东大学热科学与工程研究中心,山东济南250061
出 处:《化工学报》2013年第9期3123-3129,共7页CIESC Journal
基 金:国家自然科学基金项目(51106090);济南市高校院所自主创新项目(201202089)~~
摘 要:针对现有四分螺旋折流板换热器中心区域漏流明显的特征,提出了一种新型的六分扇形螺旋折流板换热器。建立了六分扇形螺旋折流板换热器的三维物理模型,应用Ansys CFX软件对其壳程流动与传热特性进行数值模拟,分析了不同螺旋角(10°、20°、30°、40°)和不同工况下六分扇形螺旋折流板换热器的壳侧性能,并与传统的弓形折流板换热器作对比。结果表明,六分扇形螺旋折流板可以显著减少三角区漏流现象的发生,壳程流体旋流特性较好。随着螺旋角的增大,壳侧速度场与温度场分布更加均匀,综合换热性能逐步提高。Faced with the obvious leakage flow phenomena in the heat exchanger with quarter helical baffles,a novel sextant helical baffled heat exchanger was put forward in this paper.The 3-dimensional physical model of sextant helical baffled heat exchanger was built;numerical simulation was performed with different helical angles(10°,20°,30°,40°)under different working conditions.ANSYS CFX software was used to obtain detailed fluid flow and heat transfer characteristics on the shell-side,and comparison was made between the new and the traditional segmental baffled heat exchangers.Results indicate that the leakage flow is significantly reduced with the sextant helical baffles,and shell-side rotational flow characteristics are also improved.As the helical angle increases,the velocity field and the temperature field become much uniform,so the comprehensive heat transfer performance is improved.
分 类 号:TK124[动力工程及工程热物理—工程热物理]
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