4.7 Article

A comprehensive analysis for second law attributes of spiral heat exchanger operating with nanofluid using two-phase mixture model: Exergy destruction minimization attitude

Journal

ADVANCED POWDER TECHNOLOGY
Volume 32, Issue 1, Pages 211-224

Publisher

ELSEVIER
DOI: 10.1016/j.apt.2020.12.005

Keywords

Spiral heat exchanger; Nanofluid; Two-phase mixture model; Exergy destruction; Second law efficiency

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The study focuses on the second law attributes of a counter-flow spiral heat exchanger with an Al2O3-H2O nanofluid, showing that dispersing more nanoparticles can reduce total entropy generation while increasing thermal entropy generation. Overall exergy destruction in the heat exchanger decreases significantly with increasing volume fraction, but tends to increase with flow rate increment. The second law efficiency of the heat exchanger is consistently high, with a minimum value greater than 0.84 and increasing with higher volume fraction or flow rate.
The present article focuses on the second law attributes of a counter-flow spiral heat exchanger working with an Al2O3-H2O nanofluid with employing the two-phase mixture model. To improve the cogency of the simulations, the turbulence modeling is performed using four-equation transition Shear Stress Transport (SST) model. The simulations are conducted for different nanoparticle volume fractions and nanofluid flow rates. It is shown that by dispersing further nanoparticles in the common fluid, the total entropy generation of the hot nanofluid significantly diminishes, whereas the cold water and the heat exchanger body exhibit higher thermal entropy generation. The overall exergy destruction in the heat exchanger significantly decreases by the increase of the volume fraction, while it tends to increase by the flow rate increment. For instance, an about 9.2% reduction in the overall exergy destruction is observed as the volume fraction increases from 0.01 to 0.04. All the conditions exhibit great second law efficiency so that the minimum second law efficiency is larger than 0.84, and increases with the raise of either the volume fraction or flow rate. (c) 2021 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.

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