کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
653452 | 1457511 | 2013 | 7 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Heatlines based natural convection analysis in tilted isosceles triangular enclosures with linearly heated inclined walls: effect of various orientations
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
جریان سیال و فرایندهای انتقال
پیش نمایش صفحه اول مقاله
![عکس صفحه اول مقاله: Heatlines based natural convection analysis in tilted isosceles triangular enclosures with linearly heated inclined walls: effect of various orientations Heatlines based natural convection analysis in tilted isosceles triangular enclosures with linearly heated inclined walls: effect of various orientations](/preview/png/653452.png)
چکیده انگلیسی
Natural convection in isosceles triangular enclosures with various configurations (case 1 - inverted, case 2 - straight and case 3 - tilted) is studied via heatline analysis for linear heating of inclined walls. Detailed analysis and comparison for various base angles (Ï = 45°, 60°) of triangular enclosures have been carried out for a range of fluids (Pr = 0.015 â 1000) within Ra = 103 â 105 using Galerkin finite element method. The heat flow distributions indicate conduction dominant heat transfer at low Ra (Ra = 103) for case 1 and case 2 whereas in case 3, convective heat flow is observed due to high buoyancy force. As Ra increases, enhanced thermal mixing is observed at the core of the cavity. Wall to wall heat transfer occurs at walls AB and AC due to linear heating boundary condition in all the cases. Although the distributions of fluid flow and heat flow are qualitatively similar for Ï = 45° and 60°, the intensity of fluid flow and heat flow decreases as Ï increases. Strength of fluid flow and heat flow circulation cells is found to be higher in case 3 for identical parameters. Results show that upper side wall (AC) for case 3 exhibits higher heat transfer rates whereas heat transfer rates for walls AB and AC are the same for case 1 and case 2. Also NuAB is higher for case 2 followed by case 1 and case 3 at the middle portion of wall AB. Thus to achieve high heat transfer from fluid to wall at the central region, case 2 and case 3 configurations may be recommended at high Ra (Ra = 105) and Pr, irrespective of Ï.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: International Communications in Heat and Mass Transfer - Volume 43, April 2013, Pages 39-45
Journal: International Communications in Heat and Mass Transfer - Volume 43, April 2013, Pages 39-45
نویسندگان
Tanmay Basak, R. Anandalakshmi, Monisha Roy,