عنوان المقالة:أنتقال الحرارة في الحمل المختلط في الانابيب المائلة ذات الفيض الحراري الثابت Mixed Convection Heat Transfer in Inclined Tubes with Constant Heat Flux
رائد رشاد جاسم | Raaid Rashad Jassem | 4194
نوع النشر
مجلة علمية
المؤلفون بالعربي
أحمد توفيق السامرائي , رائد رشاد جاسم , ثامر خليل ابراهيم
المؤلفون بالإنجليزي
, Thamir K. Ibrahim,Ahmed Tawfeeq Ahmed Al-Sammarraie, Raaid Rashad Jassem
الملخص العربي
Mixed convection heat transfer in inclined tubes of circular cross section has been experimentally studied for assisting, thermally developing and thermally fully developed laminar-to-turbulent air flows, under constant wall heat flux boundary condition, at Reynolds numbers (Re<2300) for the laminar and (2300<Re<4000) for transition-toturbulent air flows, and the heat flux is varied from 492 to 1442 W/m2. The mixed convection regime has been bounded by the convenient selection of Reynolds number range and the heat flux range so that the obtained Richardson number (Ri) is varied approximately from 0.146 to 1.058. The experimental rig consists of three copper tubes as test section with 600 mm heated length and length to diameter ratio (L/D= 11.8, 15.75 and 31.5). This study has investigated the effect of the heat flux, diameters and inclination angle of the tube on the mixed convection heat transfer process. In this search, the local Nusselt numbers (Nu) with the dimensionless axial distance (Z) are presented. The results have clearly shown that an increase in the Nusselt number values as the heat flux increases and as the tube inclination angle moves from (q = 60°) to (q = 30°), vice versa the Nusselt number decrease with effect of increase the length to diameter ratio (L/D). For the range of Reynolds numbers used in experiments, the maximum Nusselt number has occurred at about 30° inclination relative to the horizon. Present experimental results have a good agreement with previous results obtained for similarly tubes inclination angles. Based on the experimental results, the average Nusselt number ( Nu ) has been correlated in an empirical equation with the effect of the Rayleigh number, Reynolds number, length to diameter ratio and inclination angle. Good agreement can be seen between the experimental results and this equation.
الملخص الانجليزي
Mixed convection heat transfer in inclined tubes of circular cross section has been experimentally studied for assisting, thermally developing and thermally fully developed laminar-to-turbulent air flows, under constant wall heat flux boundary condition, at Reynolds numbers (Re<2300) for the laminar and (2300<Re<4000) for transition-toturbulent air flows, and the heat flux is varied from 492 to 1442 W/m2. The mixed convection regime has been bounded by the convenient selection of Reynolds number range and the heat flux range so that the obtained Richardson number (Ri) is varied approximately from 0.146 to 1.058. The experimental rig consists of three copper tubes as test section with 600 mm heated length and length to diameter ratio (L/D= 11.8, 15.75 and 31.5). This study has investigated the effect of the heat flux, diameters and inclination angle of the tube on the mixed convection heat transfer process. In this search, the local Nusselt numbers (Nu) with the dimensionless axial distance (Z) are presented. The results have clearly shown that an increase in the Nusselt number values as the heat flux increases and as the tube inclination angle moves from (q = 60°) to (q = 30°), vice versa the Nusselt number decrease with effect of increase the length to diameter ratio (L/D). For the range of Reynolds numbers used in experiments, the maximum Nusselt number has occurred at about 30° inclination relative to the horizon. Present experimental results have a good agreement with previous results obtained for similarly tubes inclination angles. Based on the experimental results, the average Nusselt number ( Nu ) has been correlated in an empirical equation with the effect of the Rayleigh number, Reynolds number, length to diameter ratio and inclination angle. Good agreement can be seen between the experimental results and this equation.
تاريخ النشر
02/03/2013
الناشر
European Journal of Scientific Research
رقم المجلد
97
رقم العدد
1
ISSN/ISBN
450-216X
رابط DOI
http://www.europeanjournalofscientificresearch.com
الصفحات
144-158
رابط الملف
تحميل (171 مرات التحميل)
الكلمات المفتاحية
Mixed Convection Heat Transfer, Constant Heat Flux, Inclined Tube, Diameter
رجوع