Single phase flow heat transfer characteristics of quad-channel twisted tape inserts in tubes

被引:14
作者
Dalkilic, Ahmet Selim [1 ]
Uluc, Baran [1 ]
Cellek, Mehmet Salih [2 ]
Celen, Ali [3 ]
Jumpholkul, Chaiwat [4 ]
Newaz, Kazi Salim [5 ]
Wongwises, Somchai [4 ,6 ]
机构
[1] Yildiz Tech Univ, Fac Mech Engn, Dept Mech Engn, Heat & Thermodynam Div, TR-34349 Istanbul, Turkey
[2] Bingol Univ, Fac Engn & Architecture, Dept Mech Engn, Heat & Thermodynam Div, TR-12000 Bingol, Turkey
[3] Erzincan Univ, Fac Engn, Dept Mech Engn, Thermodynam Div, TR-24100 Erzincan, Turkey
[4] King Mongkuts Univ Technol Thonburi KMUTT, Fac Engn, Dept Mech Engn, Fluid Mech Thermal Engn & Multiphase Flow Res Lab, Bangkok 10140, Thailand
[5] Univ Malaya, Fac Engn, Dept Mech Engn, Kuala Lumpur 50603, Malaysia
[6] Natl Sci & Technol Dev Agcy NSTDA, Pathum Thani 12120, Thailand
关键词
Double-pipe heat exchanger; Quad-channel twisted tape; Passive heat transfer enhancement; Single phase flow; Constant heat flux; FRICTION FACTOR CHARACTERISTICS; TRANSFER ENHANCEMENT; CIRCULAR TUBE; TURBULENT-FLOW; PRESSURE-DROP; LAMINAR-FLOW;
D O I
10.1016/j.icheatmasstransfer.2020.104835
中图分类号
O414.1 [热力学];
学科分类号
摘要
Heat transfer and pressure drop of turbulent fluid flow were studied numerically and experimentally in a quad-channel with twisted tapes placed in a circular tube under uniform heat flux boundary condition. All the tests were conducted with water as the working fluid where the turbulent flow range of Reynolds numbers were maintained at 4250 to 11000. Quad-channel twisted tapes (QCTT) were manufactured by 3D printer with the material PLA, the lengths of 50 mm, 100 mm, 200 mm with the twist ratio of 4.48. The tapes were identified with their tape/pipe length ratios (TPR) of 0.025, 0.05 and 0.1. Validation of the experimental data was performed by the comparison of the experimental results with the data from the well-known empirical correlations. Alteration of the friction factors and Nusselt numbers with the Reynolds numbers are presented in this paper. The results showed that the Nusselt number and the friction factor increased with the increasing of the length of Quri s. On the other hand, the performance evaluation criteria (PEC) should be declining with the increase of the lengths of the tapes. The evaluated temperature distributions inside the tested tubes with the inserts were plotted in order to investigate the observed data. Based on the obtained experimental data, the empirical correlations for the Nusselt number within the deviation of +/- 2% and the friction factor within the deviation of +/- 5% were developed for the practical usage.
引用
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页数:14
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