鼓泡型板式换热器是一种新型热交换器.目前其板型几何参数对板片通道内流动与传热的影响规律还不清楚.本文基于多场协同原理进行了数值研究,发现当单元体长度增大或宽度减小时,通道摩擦阻力因子f减小,综合性能评价参数PEC值增大;当单元体相对主流流动方向倾斜角为90°时,f值最小,PEC值最大.本文的研究结果对鼓泡板片传热元件的几何结构优化设计具有指导意义.
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