Enhancement of Heat Transfer Rate with a Low-Pressure Drop in Shell and Tube Heat Exchanger through Optimal Spacing of Helical Baffle

Author:

Prasad S. K.,Sinha M. K.

Publisher

Pleiades Publishing Ltd

Subject

Energy Engineering and Power Technology,Condensed Matter Physics,Modeling and Simulation,Environmental Engineering

Reference21 articles.

1. Wang, Q.W., Luo, L.Q., Zeng, M., Wang, L., Tao, W.Q., and Huang, Y.P., Shell-Side Heat Exchanger and Pressure Drop of Shell-and-Tube Heat Exchangers with Overlap Helical Baffles, J. Chem. Ind. Eng., 2005, vol. 56, no. 4, pp. 994–998 [in Chinese].

2. Xiao, J., Wang, S., Ye, S., Wang, J., Wen, J., and Tu, J., Experimental Investigation on Pre-Heating Technology of Coal Water Slurry with Different Concentration in Shell-and-Tube Heat Exchangers with Ladder-Type Fold Baffles, Int. J. Heat Mass Transfer, 2019, vol. 132, pp. 1116–1125.

3. Gu, X., Luo, Y., Xiong, X., Wang, K., and Wang, Y., Numerical and Experimental Investigation of the Heat Exchanger with Trapezoidal Baffle, Int. J. Heat Mass Transfer, 2018, vol. 127, pp. 598–606.

4. Wen, et al., Empirically Explored the Performance of an STHE with Different Baffles. (The authors reported that the increase in the shall-side pressure loss was about 0.911–9.084 kPa, and the U improved by 18.1–22.5% in the case of using the ladder-type fold baffles.)

5. Chen, J., Lu, X., Wang, Q., and Zeng, M., Experimental Investigation on Thermal-Hydraulic Performance of a Novel Shell-and-Tube Heat Exchanger with Unilateral Ladder Type Helical Baffles, Appl. Therm. Eng., 2019, vol. 161, p. 114099.

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