Abstract

Thermal efficiency development in a square channel heat exchanger attached with sinusoidal wavy surface is presented numerically. The affectation of flow attack angles ( α = 30°, 45°, and 60°), flow directions or sinusoidal wavy surface arrangements (V-apex directing downstream named “V-Downstream” and V-apex indicating upstream named “V-Upstream”), and amplitude ratios (blockage ratios = 0.10, 0.15, 0.20, and 0.25) for heat transfer and flow structure are examined for laminar flow regime ( Re = 100–1000). The physical model for the present investigation is validated with the correlation data. The current problem is resolved with the finite volume approach (semi-implicit method for pressure-linked equations algorithm). The computational information is illustrated in forms of flow topology and heat transfer mechanism in the square channel heat exchanger. The understanding of flow topology and heat transfer mechanism in the square channel heat exchanger is important knowledge to develop the heat transfer coefficient in the heat exchanger. The present of the sinusoidal wavy surface in the square channel heat exchanger can expand the heat transfer coefficient greater than the plain channel in all examples ( Nu/ Nu0 > 1). The maximal heat transfer rate is around 5.58 times above the plain square unit with the optimal performance around 1.98.

Highlights

  • The development for thermal effectiveness in several kinds of heat exchangers and many engineering devices had been performed by many researchers

  • The fine mesh is applied near the square channel walls, where we extremely found the change of the velocity and thermal boundary layers

  • Figure 20. f/f0 with BR of the square channel heat exchanger (SCHE) inserted with sinusoidal wavy surface (SWS) at a = 30° for (a) VDA and (b) VUA

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Summary

Introduction

The development for thermal effectiveness in several kinds of heat exchangers and many engineering devices had been performed by many researchers. The air velocity is presented in terms of the Reynolds number, while the pressure loss and heat transfer rate are reported in forms of the friction factor and Nusselt number, respectively. The physical model of the SCHE installed with SWS is validated to ensure that the numerical model has more reliance to presume flow topology and heat transfer mechanism of the present problem.

Results
Conclusion

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