首页> 外文会议>International Conference on Boiling Heat Transfer(ICBHT 2003); 20030504-08; Montego Bay(JM) >STUDY OF POTENTIAL ENHANCEMENT OF HEAT TRANSFER BY BUBBLE ENTRAINMENT IN HORIZONTAL FLOW BOILING
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STUDY OF POTENTIAL ENHANCEMENT OF HEAT TRANSFER BY BUBBLE ENTRAINMENT IN HORIZONTAL FLOW BOILING

机译:水平沸腾中气泡起泡强化传热的研究

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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:解释环形流沸腾过程中传热系数实验行为的传统方法是采用强制对流蒸发过程,只要施加的热通量提示发生核沸腾,就会叠加核沸腾的影响。尽管传统方法过去曾受到挑战,但由于施加的热通量,夹带气泡的生长对传热有重大贡献的可能性已被忽略。可能存在抑制核沸腾的情况,但是液膜内的过热仍然足以使较大的夹带气泡生长。在分析这种可能性时,了解薄膜中气泡的大小和位置至关重要。在室温和接近大气压的压力下,在空气-水环路中的绝热环形流动过程中,从清晰的测试部分获得的背光图像的使用表明存在夹带的气泡,直径范围在大约10μm至200μm之间。通过高分辨率的数字成像和图像处理软件,可以在管子的侧面探索这些气泡的尺寸分布。气泡统计的行为表明夹带机制是发生在干扰波中的折叠动作。使用脉冲激光诱导的荧光技术(PLIF)通过液膜的横截面图像说明了夹带事件。将提供合适的气泡生长传热机制模型,并以实验气泡信息作为输入,以与壁上的异质成核相比,确定该机制的潜在效果。

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