An experimental investigation on the effect of new continuous core-baffle geometry on the mixed convection heat transfer in shell and coil heat exchanger

被引:26
作者
Andrzejczyk, R. [1 ]
Muszynski, T. [1 ]
机构
[1] Gdansk Univ Technol, Narutowicza 11-12, PL-80233 Gdansk, Poland
关键词
Heat transfer enhancement; Shell and coil heat exchanger; Heat transfer coefficient; Nusselt number; PRESSURE-DROP; HELICAL-COIL; TRANSFER ENHANCEMENT; THERMAL PERFORMANCE; PIPE; FLOW; CONDENSATION; MINICHANNELS; INSERTS;
D O I
10.1016/j.applthermaleng.2018.03.003
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the article, the authors presented the influence of continuous core-baffle geometry at mixed convection heat transfer in shell and coil heat exchanger. Experiments were carried out for a large power range, i.e. from 100 W to 1200 W and mass flow rates ranging from 0.01 kg/s to 0.025 kg/s. During the experiments, the mass flow rate of cooling water, the temperature of water at the inlet and outlet as well as the wall temperature of the coil (at 6 points over the coil's circumference) and the water temperature in the jacket of the exchanger (at 10 points along the shell height) were measured. The article confirmed that new form of continuous baffle geometry can successfully enhance heat transfer, but rather for small values of mass flow rates. It was also noted that the inlet/outlet configuration has significant influences on the fluid flow as well as temperature distribution at the jacket of the heat exchanger. The new experimental Nusselt numbers correlation at the shell side of the heat exchanger with continuous core-baffles was presented.
引用
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页码:237 / 251
页数:15
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