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An electrochemical investigation of mass transfer in a pipe and a simplified bifurcation model.

机译:管道中传质的电化学研究和简化的分叉模型。

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A novel technique was used to fabricate nickel flow models of a straight pipe and a Y-bifurcation. These were used to obtain integral mass transfer coefficients by the electrochemical technique with the ferri-ferrocyanide system at Reynolds numbers ranging from 250 to 8600, at the four Schmidt numbers of 1310, 2470, 3100 and 5655. For the straight pipe, good agreement was obtained with previously reported mass transfer correlations. As the Schmidt number increased, the effect of transition from laminar to turbulent flow on mass transfer was delayed to progressively higher Reynolds numbers. With the Y-bifurcation model, possible flow separation and the formation of a new mass transfer boundary layer in the daughter branches significantly influence the mass transfer behavior.; The electrochemical technique has been used to obtain transient mass transfer coefficients for smooth pipes. In contrast to the analytical solution of the corresponding heat transfer problem, two distinct transient periods are observed. The first is controlled by chemical reaction kinetics at the surface, followed by the diffusion-controlled period in agreement with the heat transfer solution. The transfer rate for laminar flow is then proportional to (D/t)1/2, in accordance with Higbie's penetration theory. In turbulent flow, the transient mass transfer rate, during the second transient period, is proportional to Re1/4(D/t)1/2, higher than in laminar flow.; The laser photochromic tracer method provided velocity and wall shear stress values in the plane of symmetry of a UV-transparent Plexiglas bifurcation model similar to that used in the mass transfer experiments at Reynolds numbers 500, 600, and 750. A novel copper electrodeposition technique has been used to obtain time-averaged convective local mass transfer coefficients in a straight pipe and a simplified bifurcation model. Laminar flow results for the pipe are in good agreement with the analytical Leveque solution. In the bifurcation, higher mass transfer coefficients along the inner wall and lower ones along the outer wall were observed. Both coefficients converge towards the same value further downstream. Within the branches, mass transfer and wall shear stress follow similar patterns both on the inner and outer walls. It was found that StSc2/3 and Cf/2 demonstrate analogous behavior.; The lower transfer phenomena, both momentum and mass, along the outer wall of the branches are coincident with the localization of atherosclerotic lesions and arterial plaques.
机译:一种新颖的技术被用来制造直管和Y叉的镍流模型。通过电化学技术,使用雷亚铁-亚铁氰化物体系,在雷诺数为250至8600的四个施密特数为1310、2470、3100和5655的情况下,使用这些参数来获得积分传质系数。对于直管,良好的一致性是通过先前报道的传质相关性获得。随着Schmidt数的增加,从层流到湍流过渡对传质的影响被延迟到逐渐升高的雷诺数。在Y分叉模型中,可能的流动分离和子分支中新的传质边界层的形成会显着影响传质行为。电化学技术已用于获得光滑管的瞬态传质系数。与相应的传热问题的解析解决方案相比,观察到了两个不同的瞬态周期。首先是通过表面的化学反应动力学来控制,然后是与传热溶液一致的扩散控制时间。然后,根据Higbie的渗透理论,层流的传输速率与(D / t) 1/2 成比例。在湍流中,第二个瞬态期间的瞬态传质速率与Re 1/4 (D / t) 1/2 成正比,高于层流流。;激光光致变色示踪法在透明的紫外线有机玻璃分叉模型的对称面上提供了速度和壁切应力值,类似于雷诺数为500、600和750的传质实验中使用的模型。一种新颖的铜电沉积技术具有在直管中使用时间平均对流局部传质系数和简化的分叉模型。管道的层流结果与Leveque分析解决方案非常吻合。在分叉处,观察到沿内壁的传质系数较高,沿外壁的传质系数较低。这两个系数在下游进一步收敛于相同的值。在分支内,内壁和外壁上的传质和壁剪应力遵循相似的模式。发现StSc 2/3 和C f / 2表现出相似的行为。沿着分支的外壁的较低的转移现象,包括动量和质量,都与动脉粥样硬化病变和动脉斑块的定位一致。

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