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Flow and Heat Transfer of Quiescent Non-Newtonian Power-Law Fluid Driven by a Moving Plate: An Integral Approach

机译:由移动板驱动的静态非牛顿电力法流体的流量和传热:一种整体方法

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The problem of boundary layer flow and heat transfer from a plate moving in a quiescent non-Newtonian power law fluid medium is solved numerically to obtain results showing the effects of power-law index and Reynolds number on friction and heat transfer coefficients. A decrease in friction coefficients and an increase in heat transfer coefficients is observed for power-law liquids in comparison with water. Further in the case of a power-law liquid, an increase in the velocity of the plate also produces a reduction in drag and an increase in heat transfer. Compared to a Newtonian liquid, the friction coefficient decreases by 57% for a non-Newtonian liquid of power-law index, n = 0.568 at Re=2000. By increasing the Reynolds number to 10000, the friction coefficient decreases to 66% in comparison with a Newtonian liquid.
机译:数字地解决了从静态非牛顿电力法流体介质中移动的板的边界层流量和热传递的问题,以获得显示电力法指数和雷诺数对摩擦和传热系数的效果的结果。与水相比,对于电力法液体,观察到摩擦系数的降低和传热系数的增加。此外,在动力法液体的情况下,板的速度的增加也会产生减少阻力和热传递的增加。与牛顿液体相比,摩擦系数降低57%,对于电力法指数的非牛顿液,n = 0.568,RE = 2000。通过将雷诺数增加到10000,与牛顿液体相比,摩擦系数降至66%。

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