Pressure drop study of two-phase flows under condensation within capillary tubes

Q1 Chemical Engineering International Journal of Thermofluids Pub Date : 2025-03-11 DOI:10.1016/j.ijft.2025.101169
K. G. Domiciano , M. B. H. Mantelli , M. Mameli , S. Filippeschi
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Abstract

In the present study, an experimental investigation of pressure drops in two-phase flows within capillary tubes operating at low mass flow rates under condensation conditions was conducted. The primary objective was to understand the mechanics driving such flows to support the design of condensers for small two-phase devices, such as miniature loop heat pipes. A simple yet innovative experimental setup was developed, wherein the flows, similar to those in heat pipe technologies, were passively induced by vapor pressure. Pressure drops in two-phase flows under diabatic conditions were measured. Water and ethanol were tested, with mass flow rates below 6 × 10⁻⁵ kg/s and mass fluxes ranging from 15.5 to 209.3 kg/m²s. Copper and high-quality PVC capillary tubes with diameters between 0.446 mm and 1.010 mm were employed. Under diabatic conditions, the vapor entered the tubes with an initial vapor quality of one and condensed as it traveled through the tubes, leaving with vapor qualities between approximately 70 % and 90 %. In some cases, the condensed liquid coalesced into large plugs that completely filled the tube's cross-section, leading to confined flow conditions. These liquid plugs required higher vapor pressures to be pumped along the tube. Consequently, the pressure drop behavior was highly dependent on the flow regime. Lower pressure drops were observed when the vapor flowed at high velocities, causing the liquid to disperse into small droplets. Conversely, higher pressure drops occurred when the condensate formed blockages within the tube. The pressure drops in the flow ranged from 958 Pa to 75.4 kPa for water and 524 Pa to 59.8 kPa for ethanol. These values were consistently between the single-phase vapor and liquid pressure drops, typically closer to the latter. Notably, the observed pressure drops were significantly lower than those predicted by conventional literature correlations for two-phase flows. Furthermore, the study discusses the critical roles of pressure drops induced by fluid phase changes and the influence of capillary forces due to the confined liquid flows.
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毛细管内冷凝条件下两相流压降研究
在本研究中,对冷凝条件下低质量流量毛细管内两相流的压降进行了实验研究。主要目标是了解驱动这种流动的机制,以支持小型两相设备(如微型环路热管)的冷凝器设计。开发了一种简单而创新的实验装置,其中的流动类似于热管技术,被动地由蒸汽压诱导。测量了非绝热条件下两相流的压降。对水和乙醇进行了测试,其质量流率低于6 × 10⁻- 5 kg/s,质量通量在15.5至209.3 kg/m²s之间。采用直径在0.446 mm ~ 1.010 mm之间的铜和优质PVC毛细管。在绝热条件下,蒸汽进入管道时的初始蒸汽质量为1,并在穿过管道时冷凝,留下的蒸汽质量约为70%至90%。在某些情况下,冷凝液体凝聚成大塞,完全填满了管道的横截面,导致流动受限。这些液体塞需要沿着管道泵送更高的蒸汽压力。因此,压降行为高度依赖于流动形式。当蒸汽以高速流动时,观察到较低的压降,使液体分散成小液滴。相反,当冷凝物在管内形成堵塞时,会出现更高的压降。水的压降范围为958 ~ 75.4 kPa,乙醇的压降范围为524 ~ 59.8 kPa。这些值在单相蒸汽压降和液相压降之间一致,通常更接近后者。值得注意的是,观察到的压降明显低于传统文献中两相流相关预测的压降。此外,还讨论了流体相变引起的压降和由于流体流动受限而引起的毛细力的影响的关键作用。
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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