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Lattice Boltzmann simulation of convective heat transfer of non-Newtonian fluids in impeller stirred tank

机译:叶轮搅拌槽内非牛顿流体对流换热的格子Boltzmann模拟

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Lattice Boltzmann simulation of convective heat transfer of non-Newtonian fluids in an impeller stirred tank is performed. The curved and moving boundary methods combined with the unknown-index algorithm are used to solve the flow and thermal fields induced in a cold tank by an oscillating hot impeller. For a given maximum radius of the blades, the simulation results show that a rectangular impeller of large aspect ratio induces stronger heat transfer effect on the tank walls than the small aspect ratio. This is because the latter would cause worse field synergy than the former, i.e. the induced local velocities of fluid are mostly perpendicular to the temperature gradients. The convection effects on the tank walls are also improved as the oscillation amplitude of impeller increases until the swept areas of impeller are close to whole azimuth of the tank, i.e., oscillation amplitude of 90°. The maximum Nusselt number on the tank walls for power-law fluid flows of n=0.7,1 and 1.5 occurs at oscillation amplitude of 75°. Finally, it is found that the heat transfer effect on the tank walls is reduced as the power-law index of fluid increases.
机译:对叶轮搅拌罐中非牛顿流体的对流传热进行了格子Boltzmann模拟。曲线和运动边界方法与未知指标算法相结合,用于解决振荡热叶轮在冷罐中引起的流场和热场。对于给定的最大叶片半径,仿真结果表明,长径比大的矩形叶轮比低长径比对罐壁的传热效果更强。这是因为后者将比前者引起更差的场协同作用,即,流体的感应局部速度大多垂直于温度梯度。随着叶轮的振荡幅度增加,直到叶轮的扫掠区域接近于罐的整个方位角,即90°的振荡幅度,对箱壁的对流效果也得到改善。幂律流体流在油箱壁上的最大努塞尔数为n = 0.7,1和1.5,出现在75°的振荡幅度上。最后,发现随着流体的幂律指数的增加,在箱壁上的传热效果降低。

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