Abstract

This work numerically investigates how the boundary conditions of a heated sessile water droplet should be defined in order to include effects of both ambient and internal flow. Significance of water vapor, Marangoni convection, separate simulations of the external and internal flow, and influence of contact angle throughout drying is studied. The quasi-steady simulations are carried out with Computational Fluid Dynamics and conduction, natural convection and Marangoni convection are accounted for inside the droplet. For the studied conditions, a noticeable effect of buoyancy due to evaporation is observed. Hence, the inclusion of moisture increases the maximum velocities in the external flow. Marangoni convection will, in its turn, increase the velocity within the droplet with up to three orders of magnitude. Results furthermore show that the internal and ambient flow can be simulated separately for the conditions studied, and the accuracy is improved if the internal temperature gradient is low, e.g. if Marangoni convection is present. Simultaneous simulations of the domains are however preferred at high plate temperatures if both internal and external flows are dominated by buoyancy and natural convection. The importance of a spatially resolved heat and mass transfer boundary condition is, in its turn, increased if the internal velocity is small or if there is a large variation of the transfer coefficients at the surface. Finally, the results indicate that when the internal convective heat transport is small, a rather constant evaporation rate may be obtained throughout the drying at certain conditions.

Highlights

  • Evaporation of sessile droplets is vital for a number of applications

  • The appearance of Marangoni convection in water droplets has been questioned in experimental investigations, with results indicating a suppression of Marangoni convection [4]

  • Conduction and natural convection inside the droplet is simulated simultaneously with the external flow, including thermal effects of evaporation, and the average evaporation rate on the droplet surface is chosen as key variable, see Table 1

Read more

Summary

Introduction

Evaporation of sessile droplets is vital for a number of applications. Dropwise evaporative cooling is, for example, often used in electronic industries, nuclear thermal management and metallurgics. A comparatively efficient way to determine the rate of evaporation from this surface is to apply an average or locally dependent Nu together with the heat and mass transfer analogy [14] With this approach the air and water domains can be simulated separately and the influence of vapor in the external flow is disregarded. The inclusion of vapor due to evaporation will increase the computational complexity but as long as the heat and mass transfer coefficient can be regarded as relatively independent of the change in temperature at the surface, i.e. change due to latent heat or internal temperature distribution, it is still possible to simulate the domains separately This enables, for example, simulation of various internal flow mechanism and particle transport without the added load of the external flow. The computation of the heat and mass transfer coefficients is compared with correlations from literature and the results are verified through comparison between methods for calculation of evaporation rate

Theory
Interface boundary conditions
Model setup
Results
Mesh convergence
External flow
Internal flow
Coupling of internal and external flow
Conclusions
Compliance with ethical standards
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call