放置可移動擾動粒子在一水平加熱銅板上對FC-72池沸騰熱傳增強研究

Abstract

本論文針對放置可移動擾動粒子於加熱銅板上對FC-72池沸騰熱傳增強實驗研究。可移動顆粒放置於加熱銅板表面上並且由一個四方型的壓克力圍牆圍住，來防止可移動顆粒不會因為液體的流動，導致可移動顆粒被沖離了加熱銅板表面。在實驗中探討顆粒種類、顆粒直徑和顆粒的數量。在實驗參數範圍上，熱通量q從0.1到6 W/cm2，顆粒直徑有1.0和1.5 mm，顆粒的數量從100到1800(對於直徑為1.0 mm的顆粒)和100到800(對於直徑為1.5 mm的顆粒)。 實驗數據以壁過熱度對應輸入的熱通量及熱傳係數表示，比較對於光滑加熱銅塊下熱傳增強的表現。放置可移動擾動銅粒子相較於光滑表面對於FC-72之池沸騰熱傳係數有430%的增強效果。而對於放置可移動擾動不銹鋼粒子相較於光滑表面，整體的沸騰熱傳係數有530%的增強效果。甚至當加熱銅板上覆蓋滿顆粒(最多鋪滿兩層)對於整體的散熱效果有明顯的增強。但在高熱通量時，散熱效果有降低的趨勢，特別對於放置直徑1.5 mm的顆粒，散熱效果降低的趨勢很明顯。由數據呈現的圖形可得，熱傳增強的表現會因其不同的參數搭配而有不同的增強效果，理想且良好的熱傳增強表現在於適當的顆粒種類、顆粒直徑和顆粒數量的搭配。 由數據呈現的結果指出，放置可移動擾動粒子於加熱銅板上後對於整體的散熱效果有增強的效果也有降低的效果。在高熱通量時，散熱效果有明顯降低的現象。

An experiment is carried out here to investigate how the saturated pool boiling heat transfer of liquid FC-72 over a horizontal heated copper plate of 3×3 〖cm〗^2 in surface area is affected by placing metallic particles above the surface, intending to explore the possible pool boiling heat transfer enhancement by the moving particles. Both copper and stainless steel particles are tested. The particles are freely placed above the heated plate with a rectangular fence surrounding the plate so that the particles can be moved by the force induced by the boiling flow without being blown away. In the experiment, the imposed heat flux is varied from 0.1 to 6 W/cm2 for the diameter of the particles fixed at 1.0 and 1.5 mm. Besides, the total particle number placed on the plate ranges from 100 to 1800 and from 100 to 800 respectively for the small and large particles. The measured data are presented in terms of boiling curves and boiling heat transfer coefficients for the heating surface with the presence and absence of the particles. The experimental parameters include the imposed heat flux level and the size, material and number of the particles. The data obtained from the present study for the saturated pool boiling indicate that placing the movable particles can significantly increase the pool boiling heat transfer coefficient of FC-72 at low and medium heat fluxes (wall superheats). For the copper particles the enhancement can be up to 430% over that for a bare surface for a certain combination of the experimental parameters. The best enhancement can be as high as 530% for the stainless steel particles. Even when more than one layer of particles are placed on the plate relatively significant boiling heat transfer enhancement can still be obtained. However, the boiling heat transfer enhancement varies nonmonotonically with the particle diameter, number and material and the heat flux applied, reflecting the complex mutual influences of the movable particles and bubble motion near the heated surface. An optimal boiling heat transfer enhancement could be procured by a suitable choice of the experimental parameters. Besides, the wall superheat for the incipient boiling can be substantially reduced by the moving metallic particles. However, at high heat flux (wall superheat) placing the particles on the plate can greatly reduce the boiling heat transfer especially for the large particles. The results from the visualization of the boiling flow over the copper plate indicate that placing the movable particles above the plate results in two opposite effects of enhancing and retarding the boiling heat transfer. At high heat flux the retarding effect is strong.