论文标题
在偏心环形管中的层流对流,用于热依赖性非牛顿流体
Laminar mixed convection in an eccentric annular horizontal duct for a thermodependent non-Newtonian fluid
论文作者
论文摘要
目前的工作重点是研究水平环形偏心管中纯粘性剪切液的混合对流。内部和外部圆柱体以恒定和均匀的热通量密度加热。这项工作的目的是研究偏心率变化,流体的流变行为以及流变参数的热依赖性对流动重组和由浮力引起的热分层的影响。在加热区的入口处,假定动态状态建立并均匀。使用具有隐式方案的有限差方法来数值求解。由自然对流引起的次级方位流动在入口截面的下游发展。该流程在管道的给定部分上产生热场的分层,从而从入口下游加剧。另一方面,随着加热墙附近温度的升高,一致性下降会产生一个离心的径向流向墙壁。偏心率的存在导致对主要动态场和热场的分层产生显着影响。两例向上和向下偏心率的情况得到治疗。这些表明向上移动会增加热场的分层,而在向下移位的情况下,分层开始从一定程度的怪异范围中削弱。这是可能的工业应用方面的重要结果。我们确实可以得出结论,在同心加热环形导管的情况下,在实验中观察到适当的向下偏心率可以减少热分层[1],当时该分层是不可取的。这种偏心率的选择取决于流体的流变和热特性。
The present work focuses on the study of mixed convection of a purely viscous shear-thinning fluid in a horizontal annular eccentric duct. The inner and outer cylinders are heated with constant and uniform heat flux densities. The objective of this work is to study the effect of the variation of eccentricity, rheological behavior of the fluid as well as the thermodependency of the rheological parameters on the reorganization of the flow and thermal stratification caused by the buoyancy forces. At the entrance of the heating zone, the dynamic regime is assumed to be established and the temperature profile uniform. The conservation equations are solved numerically using a finite difference method with implicit schemes. A secondary azimuthal flow, induced by natural convection, develops downstream of the inlet section. This flow creates a stratification of the thermal field on a given section of the duct, which intensifies downstream from the entrance. On the other hand, the decrease in consistency with increasing temperature near the heated walls produces a centrifugal radial flow towards the walls. The presence of an eccentricity induces in turn a significant effect on the main dynamic field and the stratification of the thermal field. Two cases of upward and downward eccentricity are treated. These show that an upward shift increases the stratification of the thermal field, while the stratification begins to weaken from a certain amount of eccentricity in the case of downward shift. This represents an important result in terms of possible industrial applications. We may indeed conclude that an appropriate choice of downward eccentricity can reduce the thermal stratification, observed experimentally in the case of a concentric heated annular duct [1], when this stratification is undesirable. The choice of this eccentricity depends on rheological and thermal properties of the fluid.