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1. 浙江水利水电学院 先进换热与能源应用研究所
2. 浙江盾安热工科技有限公司
3. 丹佛斯板式换热器有限公司
纸质出版日期:2024,
移动端阅览
魏文建, 徐国梁, 张志锋, 等. 板式换热器板内两相流动分配特性分析及优化[J]. 制冷学报, 2024,45(1).
WEI WENJIAN, XU GUAOLIANG, ZHANG ZHIFENG, et al. Flow Characteristics and Optimization of Two-phase Flow Distribution over Plate Surface of Brazed-Plate Heat Exchanger. [J]. Journal of refrigeration, 2024, 45(1).
魏文建, 徐国梁, 张志锋, 等. 板式换热器板内两相流动分配特性分析及优化[J]. 制冷学报, 2024,45(1). DOI: 10.3969/j.issn.0253-4339.2024.01.046.
WEI WENJIAN, XU GUAOLIANG, ZHANG ZHIFENG, et al. Flow Characteristics and Optimization of Two-phase Flow Distribution over Plate Surface of Brazed-Plate Heat Exchanger. [J]. Journal of refrigeration, 2024, 45(1). DOI: 10.3969/j.issn.0253-4339.2024.01.046.
气液两相流体板内均匀流动分配是影响制冷用钎焊板式换热器性能的重要因素。本文通过计算流体力学数值模拟软件对两相制冷剂R410A在人字波和点波板内流动分配特性进行了研究,对比分析了两种板型压力分布、速度分布和液相体积比分布,发现人字波板压力、速度和液相分布相对均匀,板中心速度和液相分布略高于两侧,而点波板呈现进出口近侧流速显著高于远端而液相分布显著低于远端的分布特点。提出了用当量断面平均两相流量偏差和平均液相流量偏差对板内流动分配均匀性进行评价。结果表明:人字波板较点波板,气液两相侧向流动和分配较好,二者平均两相流量偏差分别为14.2%和39.6%,平均液相流量偏差分别为15.6%和41.3%。分析表明圆型点波结构流动方向上存在直通截面,侧向流动弱化,因气液流速差异导致两相过早分离,造成气相短路。能够控制直通截面大小和产生二次涡阶结构的“鱼鳞”点波结构可有效增强侧向扰动,改善点波板的气液两相表面流动和分配均匀性,其平均两相流量偏差和平均液相流量偏差分别为7.6和8.9%。
The homogenous distribution of liquid and vapor over a plate surface is a key factor affecting the performance of brazed-plate heat exchangers in refrigeration and air-conditioning units. The two-phase flow and distribution over the plate surface were investigated with R410A fluid using computational fluid dynamics (CFD) simulation software. The distributions of pressure
velocity
and liquid volumetric fraction were comparatively analyzed. It was observed that the pressure
velocity
and liquid phase were distributed comparatively evenly for the herringbone plate. The velocity and liquid volumetric fraction along the plate centerline were slightly higher than those along the edges. However
for the dimpled plate
the velocities in the proximal zone were significantly higher than those in the distal zone
which is opposite to the distribution of liquid volumetric fraction. New methods called the mean two-phase flow deviation (MTFD) and mean liquid flow deviation (MLFD) at the nominal section were proposed to evaluate the maldistribution of fluid flow over the plate surface. The results indicated that the distribution and sideways flow were better for the herringbone plate than for the dimple plate. The MTFD values were 14.2% and 39.6%
and the MLFD values were 15.6% and 41.3% for the herringbone and dimple plates
respectively. It was determined that the bypass section existed in the flow direction for the round dimple plate
which led to poor sideways flow and earlier separation between the vapor and liquid. The proposed boomerang dimple plate pattern
similar to fish skin
can improve the two-phase flow distribution over the plate surface because it can reduce the size of the bypass section and generate vortices under a concave shape. The new geometry can enhance turbulence and promote the two-phase fluid to move sideways effectively. The MTFD and MLFD values were 7.6% and 8.9%
respectively.
均匀分配数值模拟板式换热器蒸发器制冷剂
even distributionnumerical simulationplate heat exchangerevaporatorrefrigerant
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