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Numerical solution for laminar mixed convection in a horizontal annular duct: temperature-dependent viscosity effect

机译:水平环形管道中层流混合对流的数值解:取决于温度的粘度效应

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摘要

The influence of free convection and variable viscosity on forced laminar flow of a Newtonian fluid in a horizontal annular duct is investigated. The inner and outer cylinders are subjected to a constant heat flux density. At the entrance of theannular duct, the flow is fully developed and the temperature profile is uniform. The Prandtl and Boussinesq hypothesis were adopted. The continuity equation and the three-dimensional parabolized form of the momentum and energy equations are solvednumerically using finite differences. Near the entrance section, forced convection is the dominant mechanism. Further downstream, the fluid heats up and buoyancy becomes more important. The fluid near the walls is warmer, and therefore lighter than thefluid in the central part of the annular space; it therefore flows upward along the walls. A continuity requires a downflow of the heavier fluid between the two cylinders. This secondary flow modifies the structure of the dynamic and thermal fields. Thenumerical results show that a decrease in fluid viscosity with temperature leads to: (i) an increase in axial velocity in the upper part of the annular duct and a decrease in the lower part; (ii) a rise in the secondary flow intensity; (iii) a reductionin temperature difference between the upper and lower parts of a cylinder; (iv) an increase of the overall heat transfer coefficient.
机译:研究了自由对流和可变粘度对水平环形管道中牛顿流体强迫层流的影响。内圆柱和外圆柱承受恒定的热通量密度。在环形管道的入口处,气流充分展开,温度分布均匀。采用了Prandtl和Boussinesq假设。连续方程和动量和能量方程的三维抛物线形式使用有限差分进行数值求解。在入口附近,强制对流是主要机制。在更下游,流体变热,浮力变得更加重要。壁附近的流体较热,因此比环形空间中心部分的流体更轻。因此,它沿着墙壁向上流动。连续性要求较重的流体在两个气缸之间向下流动。该二次流改变了动态和热场的结构。数值结果表明,流体粘度随温度的降低而导致:(i)环形管道上部的轴向速度增加而下部的轴向速度减少; (ii)二次流动强度的增加; (iii)减小气缸的上部和下部之间的温差; (iv)整体传热系数的增加。

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