Rayleigh-Bénard convection of a gas-vapor mixture with abnormal dependence of thermal expansion coefficient on temperature

https://doi.org/10.1016/j.icheatmasstransfer.2021.105245Get rights and content

Abstract

In order to reveal basic characteristics of Rayleigh-Bénard convection (RBC) of a gas mixture, which has abnormal dependence of thermal expansion coefficient on temperature, we presented a direct numerical simulation on RBC of a gas mixture of oxygen and cyclohexane near its maximum density. The influences of the density inversion parameter and the Rayleigh (Ra) number on the critical conditions of the flow onset and destabilization were analyzed. The flow evolution with Ra was exhibited. The results show the critical value of Rayleigh number of the flow onset is approximately proportional to the fourth power of the thickness of the upper stable sublayer. Regardless of density inversion parameter, the flow pattern at the flow appearance always has a multicellular structure. With increasing Ra, the multicellular flow structure would be transformed into various steady flow patterns, including parallel flow and pendant pattern. When the density inversion parameter is small, the unsteady flow cells exhibit a back and forth motion along the border. However, at a large density inversion parameter, the cells swing around the centers of the flow rolls. We also found that the local Nusselt (Nu) number on the bottom depends on the flow pattern. The average Nu increases gradually with increasing Ra under a small density inversion parameter. However, an abrupt rise of the average Nu appeared under a large density inversion parameter.

Introduction

Rayleigh-Bénard convection (RBC) is a flow driven by the buoyancy force in a fluid layer with a vertical temperature gradient. Therefore, the dependence of fluid density on temperature is critical for the onset of RBC and the evolution of the flow patterns with the Rayleigh (Ra) number. Up to now, many studies on RBC of the fluids with a linear variation of the density with temperature have been carried out [[1], [2], [3], [4], [5]]. However, commonly encountered fluids with a non-monotonic variation of the density with the temperature, like cold water [6] and the gas mixture of oxygen and cyclohexane [7], have not been studied yet.

For the fluid with a linear variation of the density with temperature, convection cells of RBC appear in the fluid layer when Rayleigh number exceeds the first critical value. The spatial variation of a convection structure is referred to as flow pattern that depends on the Prandtl number of the fluid, the enclosure geometry and the boundary conditions of the fluid layer. With the increasing Ra, the buoyancy force is enhanced. When Ra exceeds the second threshold value, the steady flow pattern will destabilize and bifurcate to three-dimensional (3D) unstable flows. Furthermore, the boundaries of the stability region of the flow patterns are determined by various destabilization mechanisms, which is known as the Busse balloon [1,8].

For the fluid with a non-monotonic variation density with regard to temperature, the buoyancy force will change its sign along the direction vertical to the fluid layer due to an imposed vertical temperature gradient, which results in a variety of convection modes. Zubkov et al. [9,10] numerically calculated RBC of water near the density maximum in a cubical cavity with isothermal horizontal walls and thermally insulated vertical walls. It was found that there are six stable flow patterns at different Grashof numbers. Furthermore, the ranges of Grashof number in which all the flow patterns coexist were determined. Large and Andereck [11] performed an experiment on RBC of cold water in a cavity. It was revealed that the flow first appears in the lower unstable layer, and then penetrates the upper stable region. At onset of the flow, the flow includes parallel and transverse rolls. When the unstable layer height is much smaller than the stable layer height, the flow only partially penetrate the upper stable region, within which weak counter-rotation flows are induced. With increasing Rayleigh number, the flow undergoes a secondary transition to a hexagonal cellular or a longitudinal roll state. Hu et al. [12,13] carried out a direct numerical simulation on RBC on cold water in various vertical cavities. Results show that the density inversion has an important effect on RBC. The critical Ra for the flow onset is larger than that of the common fluid, and it increases with increasing density inversion parameter Θm. The density inversion parameter is used to describe the location of the maximum density in the cavity and is defined asΘm=TmTcThTc,where Th and Tc are the bottom and top temperatures of the liquid layer, respectively. Tm is the maximum density temperature, and Th > Tm ≥ Tc.

Furthermore, Bekezhanova [14] analyzed the stability of the equilibrium state of a horizontal cold water layer with nonlinear temperature and pressure dependences of density. Lyubimov et al. [15] determined the influence of a given heat flux boundary condition on the convection onset in a cold water layer. Furthermore, Toppaladoddi and Wettlaufer [16] studied the turbulent penetrative RBC of the density extremum fluids. It was found that the penetration depth decreases with the density inversion parameter increasing. At the same time, Nusselt (Nu) number fluctuation amplifies with increasing Ra.

The density maximum phenomenon also appears in some gas-vapor mixtures at the critical temperature Tm, such as a gas mixture of oxygen and cyclohexane. Recently, Palymskly et al. [17,18] proposed a theoretical model of RBC of oxygen and cyclohexane mixture with the density maximum., and performed a linear stability analysis. However, for simplicity they used constant thermal expansion coefficients of β = −0.01583 and 0.0030537 at T ≤ Tm and T > Tm, respectively. Recently, based on the theoretical model proposed by Palymskly et al., Yu et al. [19] carried out two-dimensional numerical simulation on RBC of the oxygen and cyclohexane mixture. The results show that the strength of RBC is suppressed with the density inversion parameter increasing. However, two-dimensional simulation cannot show 3D flow structure and reveal the formation mechanism of the flow pattern.

In this work, a series of direct numerical simulations were performed to reveal the characteristics of RBC of the oxygen and cyclohexane mixture near the density maximum point. The thermal and flow fields at different conditions were exhibited. The flow evolution with Ra was emphasized.

Section snippets

Working fluid

Oxidation of hydrocarbons has prominent economic value in chemical engineering field. Most commonly, the cyclohexene is oxidized in the liquid phase by oxygen. In this case, a gaseous mixture of cyclohexane and oxygen always appears in a reactor where there is the liquid-phase oxidation of cyclohexane. Simultaneously, few liquid cyclohexane will be left on the reactor walls. They will form a gas-liquid system with the gaseous mixture and residue liquid. When the ratio of cyclohexane to oxygen

Critical conditions of convection onset

At a small Ra, the fluid layer is quiescent and the heat transfer is conduction whether it is the Boussinesq fluid or the density extremum fluid. However, once Ra is increased to a critical value, RBC will happen. Corresponding Ra is called as the first critical Rayleigh number Racri1. In this work, the critical Rayleigh numbers are determined by the dichotomy [25]. The maximum relative deviation of the critical Rayleigh numbers is less than 1%.

Fig. 3 shows the variation of Racri1 of RBC of the

Conclusions

In this work, we presented a sets of direct numerical simulations on RBC of a gaseous oxygen and cyclohexane mixture near the density maximum in a cavity with the aspect ratio of π. From the simulation results, we can obtain the following conclusions:

  • (1)

    The first critical Ra of the RBC onset is approximately proportional to the fourth power of the dimensionless thickness of the upper stable sublayer. The critical flow pattern is a multicellular structure. Furthermore, the critical flow cell number

Declaration of competing Interest

The authors declared that there is no conflict of interest.

Acknowledgment

This work is supported by National Natural Science Foundation of China (Grant No. 51706213, 52076017) and Chongqing Basic and Frontier Research Project (No. cstc2019jcyj-msxmX0582).

References (27)

  • E. Bodenschatz et al.

    Recent developments in Rayleigh-Bénard convection

    Annu. Rev. Fluid Mech.

    (2000)
  • T. Watanabe

    Flow pattern and heat transfer rate in Rayleigh-Bénard convection

    Phys. Fluids

    (2004)
  • S. Wagner et al.

    Aspect-ratio dependency of Rayleigh-Bénard convection in box-shaped containers

    Phys. Fluids

    (2013)
  • Cited by (5)

    • Numerical investigation on Rayleigh-Bénard convection of cyclohexane-oxygen mixture near its maximum density in a rectangular container

      2023, International Journal of Thermal Sciences
      Citation Excerpt :

      The non-uniform distributions of temperature and density in Rayleigh-Bénard convection of cyclohexane/oxygen mixture can be the potential hazard factors of deflagration, but few studies pay attention to it. In previous works, the RB convection of cyclohexane/oxygen mixture near the maximum density was investigated by linear stability analysis [28] as well as numerical simulations [29,30]. The results suggest that the density inversion has a notable influence on the stability and flow structures.

    View full text