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STUDY OF POTENTIAL ENHANCEMENT OF HEAT TRANSFER BY BUBBLE ENTRAINMENT IN HORIZONTAL FLOW BOILING.

机译:水平流沸腾泡沫夹带潜在增强热传递潜力。

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The traditional approach towards explaining the experimental behavior of the heat transfer coefficient during annular flow boiling employs a forced convection evaporative process upon which the effects of nucleate boiling are superimposed whenever the applied heat flux suggests the onset of nucleate boiling. Although the traditional approach has been challenged in the past, the possibility of a significant contribution to heat transfer from the growth of entrained bubbles due to an applied heat flux has been neglected. Situations may exist in which suppression of nucleate boiling occurs, but the superheat within the liquid film is still sufficient for the growth of the larger entrained bubbles. In analyzing this possibility, knowledge of the bubble size and location within the film is fundamental. The use of backlit images obtained from clear test sections during adiabatic annular flow in an air-water loop at room temperature and pressures close to atmospheric, indicates the presence of entrained gas bubbles ranging in diameter between approximately 10 μm to 200 μm. The size distribution of these bubbles is explored at the side of the tube through high-resolution digital imaging and image processing software. The behavior of the bubble statistics indicates that the entrainment mechanism is a folding action that occurs in disturbance waves. The entrainment events are illustrated by cross sectional images of the liquid film using the pulsed laser induced fluorescence technique (PLIF). A suitable bubble growth heat transfer mechanism model will be presented with the experimental bubble information used as an input to determine the potential effect of this mechanism compared to heterogeneous nucleation at the wall.
机译:在环形沸腾期间解释传热系数的传统方法的传统方法采用强制对流蒸发过程,每当施加的热通量表明核心沸腾的发作时,核心沸腾的效果叠加。虽然过去的传统方法已经受到挑战,但忽略了由于施加的热通量引起的夹带气泡的生长的显着贡献的可能性。可能存在的情况,其中发生核心沸腾的抑制,但液体膜内的过热仍然足以使较大夹带气泡的生长。在分析这种可能性时,对薄膜内的气泡尺寸和位置的了解是基本的。在室温和靠近大气的压力下在空气 - 水环中的绝缘环形流动期间使用从清除试验部分获得的背光图像表明,夹带的气泡在直径约为10μm至200μm之间。通过高分辨率的数字成像和图像处理软件在管的侧面探讨这些气泡的尺寸分布。气泡统计的行为表明夹带机构是扰动波发生的折叠动作。夹带事件通过使用脉冲激光诱导的荧光技术(PLIF)的液膜的横截面图像来说明。将呈现合适的气泡生长传热机制模型,用作输入的实验泡沫信息,以确定与墙壁上的异质成核相比该机制的潜在效果。

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