Heat transfer behaviours of nanofluids in a uniformly heated tube

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Abstract

In the present work, we consider the problem of the forced convection flow of water– γAl2O3 and ethylene glycol– γAl2O3 nanofluids inside a uniformly heated tube that is submitted to a constant and uniform heat flux at the wall. In general, it is observed that the inclusion of nanoparticles has increased considerably the heat transfer at the tube wall for both the laminar and turbulent regimes. Such improvement of heat transfer becomes more pronounced with the increase of the particle concentration. On the other hand, the presence of particles has produced adverse effects on the wall friction that also increases with the particle volume concentration. Results have also shown that the ethylene glycol– γAl2O3 mixture gives a far better heat transfer enhancement than the water– γAl2O3 mixture.

Introduction

The thermal properties of heating or cooling fluids play a vital role in the development of new energy-efficient heat transfer equipment. However, conventional heat transfer fluids such as water, ethylene glycol and engine oils have, in general, poor heat transfer properties compared to those of most solids. In spite of considerable research and efforts deployed until today, major improvements in heat transfer capabilities have suffered a major lacking. As a result, an important need still exists to develop new strategies in order to improve the effective heat transfer behaviours of conventional heat transfer fluids.

The term ‘nanofluid’ refers to a two-phase mixture with its continuous phase being generally a liquid and the dispersed phase constituted of ‘nanoparticles’ i.e. extremely fine metallic particles of size below 100 nm. It has been shown that the thermal properties of such a nanofluid appear to be well above those of the base-fluid. In fact, some available experimental data [1], [2], [3] have shown that even with a relatively low concentration of particles, say from 1 to 5% in volume, the effective thermal conductivity of the mixture has increased by almost 20% compared to that of the base-fluid. Such an increase depends mainly on several factors such as the form and size of the particles and their concentration, the thermal properties of the base-fluid as well as those of the particles. Hence, the nanofluids can constitute an interesting alternative for advanced applications in heat transfer in the future, especially those in micro scale, see for example [8]. In spite of their potentials and advantages, these very special fluids are still in their earlier development. In fact, the first experimental works were concerned only with the measuring and the determination of the effective thermal conductivity [1], [2], [3], [4], [5], [6], [7], [9]; some also provided the effective viscosity of the nanofluids [1], [4], [9] showing that the inclusion of the nanoparticles can appreciably increase the viscosity of the resulting mixture. These works considered some current fluids, water, ethylene glycol and engine oil, and metallic particles such as γAl2O3, SiO2, TiO2 and Cu particles. It is very important to note that the amount of experimental data resulting from these studies remains, surprisingly, very limited. Furthermore, there are no available data regarding the effects of the temperature on the effective thermal conductivity and viscosity of nanofluids. It appears obvious, at the present stage, that much more works will be needed on this important issue in the future.

With regard to the thermal performance of nanofluids in confined flows, the only recent experimental works [9], [10] have provided the first empirical correlation for computing the Nusselt number in laminar and turbulent tube flows using nanofluids that are composed of water and Cu, TiO2 and γAl2O3 particles. The data as obtained from these studies have clearly shown that the suspended nanoparticles remarkably increase the heat transfer performance of the base-fluid and the suspensions have larger heat transfer coefficients than the base-fluid (pure water) under the same Reynolds number. Such an improvement becomes more important with an augmentation of the particle volume fraction. In spite of their great potentials and advantages, these new, special yet rather challenging fluids still remain in their earlier development state and much more research work will be needed in order to better understand their fluid dynamics and thermal characteristics, in particular for confined flows. In this paper, we are interested to study numerically the beneficial influence due to the inclusion of nanoparticles on the flow behaviours and the temperature field inside a uniformly heated tube.

Section snippets

Mathematical formulation and numerical method

We consider in this study the problem of the forced convection flow of a nanofluid, which is composed of water or ethylene glycol and metallic γAl2O3 nanoparticles, flowing inside a straight tube of circular cross-section, Fig. 1.Due to the extreme size of particles, it may be reasonable to suggest that such a mixture can be easily fluidized and therefore, one may assume that the motion slip between the phases, if any, would be considered negligible [11]. Also, by considering the local thermal

Results and discussion

The computer model has been successfully validated by comparing the results as obtained for the development of fluid axial velocity VZ to the corresponding analytical and numerical data by others for the classical case of an isothermal developing laminar forced convection flow in a tube [18]. Fig. 3 (introduced previously) has shown such comparison where the agreement can be qualified as very good. Fig. 4shows another comparison performed for the Nusselt number NuZ hence the heat transfer

Conclusion

In this paper, we have numerically investigated the hydrodynamic and thermal behaviours of nanofluids flowing inside a uniformly heated tube. Results have clearly shown that the inclusion of nanoparticles has produced a considerable increase of the heat transfer with respect to that of the base liquid. Such heat transfer enhancement, which appears to be more pronounced with the augmentation of the particle volume concentration, is accompanied, however, by a major drawback on the wall shear

Acknowledgements

The authors wish to sincerely thank the Natural Sciences and Engineering Research Council of Canada, the Faculty of Graduate Studies and Research of the Université de Moncton for financial support to this project, and also to the Faculty of Engineering of the Université de Moncton for allocating computing facilities.

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