工程热物理学报
工程熱物理學報
공정열물이학보
JOURNAL OF ENGINEERING THERMOPHYSICS
2009年
11期
1831-1833
,共3页
彭岚%范菊艳%唐经文%李友荣
彭嵐%範菊豔%唐經文%李友榮
팽람%범국염%당경문%리우영
分离结晶%热毛细对流%微重力%转变%临界Ma数
分離結晶%熱毛細對流%微重力%轉變%臨界Ma數
분리결정%열모세대류%미중력%전변%림계Ma수
detached solidification%thermocapillary convection%microgravity%conversion%critical Marangoni number
为了了解微重力条件下新型分离结晶生长过程中熔体热毛细对流的基本特征,利用有限差分法进行了数值模拟,熔体深径比A取1和2,自由界面无因次宽度B分别取0.05、0.075和0.1.当熔体上表面为自由表面时,得到了分离结晶Bridgman生长过程中熔体热毛细对流的流函数和温度分布.计算结果表明:当Ma数较小时,在上下两个自由表面的表面张力的驱动下,熔体内部产生了两个流动方向相反的流胞,流动为稳态流动,随着Ma数的增加,上下自由表面速度增大,温度分布的非线性增加;当Ma数超过某一临界值后,流动将转化为非稳态流动;与熔体上表面为固壁时相比,A=1时的临界Ma数减小,而A=2时的临界Ma数增大;流动失稳的物理机制是流速的变化和阻力的变化之间存在滞后.
為瞭瞭解微重力條件下新型分離結晶生長過程中鎔體熱毛細對流的基本特徵,利用有限差分法進行瞭數值模擬,鎔體深徑比A取1和2,自由界麵無因次寬度B分彆取0.05、0.075和0.1.噹鎔體上錶麵為自由錶麵時,得到瞭分離結晶Bridgman生長過程中鎔體熱毛細對流的流函數和溫度分佈.計算結果錶明:噹Ma數較小時,在上下兩箇自由錶麵的錶麵張力的驅動下,鎔體內部產生瞭兩箇流動方嚮相反的流胞,流動為穩態流動,隨著Ma數的增加,上下自由錶麵速度增大,溫度分佈的非線性增加;噹Ma數超過某一臨界值後,流動將轉化為非穩態流動;與鎔體上錶麵為固壁時相比,A=1時的臨界Ma數減小,而A=2時的臨界Ma數增大;流動失穩的物理機製是流速的變化和阻力的變化之間存在滯後.
위료료해미중력조건하신형분리결정생장과정중용체열모세대류적기본특정,이용유한차분법진행료수치모의,용체심경비A취1화2,자유계면무인차관도B분별취0.05、0.075화0.1.당용체상표면위자유표면시,득도료분리결정Bridgman생장과정중용체열모세대류적류함수화온도분포.계산결과표명:당Ma수교소시,재상하량개자유표면적표면장력적구동하,용체내부산생료량개류동방향상반적류포,류동위은태류동,수착Ma수적증가,상하자유표면속도증대,온도분포적비선성증가;당Ma수초과모일림계치후,류동장전화위비은태류동;여용체상표면위고벽시상비,A=1시적림계Ma수감소,이A=2시적림계Ma수증대;류동실은적물리궤제시류속적변화화조력적변화지간존재체후.
In order to investigate fundamental characteristics of thermocapillary convection in the detached solidification under microgravity.the finite-difference method is adopted to perform a numerical simulation for the melt of CdZnTe with the aspect ratio A=1 and 2 and the width of gap B=0.05.0.075 and 0.1.When the top surface is free surface.the distribution profiles of temperature and stream function of molten liquid can be obtained with different Marangoni numbers.The result shows that when Ma is small,there are two steady toroidal roll cells in the molten liquid counter-flows caused by the gradient of surface tension in the upper and lower free surface.With Ma increasing,the velocity on the two free surfaces and the non-linearity of temperature distribution will be improved.On the contrary,the flow is unstable when Ma exceeds the critical Ma.Compared with the top surface being solid wall,the critical Marangoni number for A=1 is lower,but for A=2 is larger.The physical mechanism of this unstable thermocapillary convection can be explained by that there is a hysteresis between the variety of the velocity and the variety of the resistance.