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Natural convection effects on heat and mass transfer in a curvilinear triangular cavity

机译:自然对流对曲线三角形空腔中传热和传质的影响

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摘要

Finite element method is used in this study to analyze the effects of buoyancy ratio and Lewis number on heat and mass transfer in a triangular cavity with zig-zag shaped bottom wall. Buoyancy ratio is defined as the ratio of Grashof number of solutal and thermal. Inclined walls of the cavity have lower temperature and concentration according to zig-zag shaped bottom wall. Enclosed space consists mostly of an absor ber plate and two inclined glass covers that form a cavity. Both high temperature and high concentrations are applied to bottom corrugated wall. Computations were done for different values of buoyancy ratio (-10 ≤ Br ≤ 10), Lewis number (0.1 ≤ Le ≤ 20) and thermal Rayleigh number (10~4 ≤ Ra_T≤ 10~6). Stream lines, isotherms, iso-concentration, average Nusselt and Sherwood numbers are obtained. It is found that average Nusselt and Sherwood numbers increase by 89.18% and 101.91 % respectively as Br increases from -10 to 20 at Ra_T = 10~5. Also, average Nusselt decreases by 16.22% and Sherwood numbers increases by 144.84% as Le increases from 0.1 to 20 at this Rayleigh number.
机译:本研究采用有限元法分析了Z形之字形底壁三角腔中浮力比和路易斯数对传热传质的影响。浮力比定义为溶解和热的格拉斯霍夫数之比。根据Z字形底壁,空腔的倾斜壁具有较低的温度和浓度。封闭的空间主要由一个吸收板和两个形成空腔的倾斜玻璃盖组成。高温和高浓度都适用于底部波纹壁。针对不同的浮力比(-10≤Br≤10),刘易斯数(0.1≤Le≤20)和热瑞利数(10〜4≤Ra_T≤10〜6)进行计算。获得流线,等温线,等浓度,平均努塞尔和舍伍德数。发现当Ra_T = 10〜5时,Br从-10增加到20,平均Nusselt和Sherwood数分别增加89.18%和101.91%。同样,在此瑞利数下,当Le从0.1增加到20时,平均Nusselt减少16.22%,Sherwood数目增加144.84%。

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