کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
667134 1458498 2016 14 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
The influence of inclination angle on void fraction and heat transfer during condensation inside a smooth tube
ترجمه فارسی عنوان
تأثیر زاویه گرانشی بر فضای خالی و انتقال گرما در طول تراکم در داخل یک لوله صاف
کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی جریان سیال و فرایندهای انتقال
چکیده انگلیسی


• Measured void fractions during condensation at different inclination angles.
• Heat transfer coefficients with void fractions at different inclination angles.
• Inclination relationship between void fractions and heat transfer coefficients.

Most work in literature on condensation in tubes has been done for smooth tubes in the horizontal and vertical configurations. Recent experimental works with condensation at different inclination angles showed that the heat transfer characteristics were a function of inclination angle. These works were limited to heat transfer and pressure drop measurements with visual observations. However, no work has been done on measuring the void fractions during condensation at different inclination angles. The purpose of this study was to measure void fractions and heat transfer coefficients during condensation for tube inclinations ranging from vertical downwards (−90°) to vertical upwards (90°) at a saturation temperature of 40 °C. Measurements were taken in an experimental set-up in which condensation occurred on the inside of a test section. The test section was a circular tube with an inner diameter of 8.38 mm and a heat transfer length of 1.488. The refrigerant used was R134a, and the void fractions were measured using two capacitive void fraction sensors. Mass fluxes ranging from 100 to 400 kg/m2 s and vapour qualities ranging from 10–90% were considered. Heat transfer coefficients were also compared with void fractions. It was found that at combinations of low mass fluxes and vapour qualities, void fraction and heat transfer were significantly affected by changes in inclination angle. Generally, void fractions and heat transfer coefficients increased with downward inclination angles with an optimum angle between −10° and −30° (downward flow). At some intermediate mass flux and vapour quality conditions, the void fraction and heat transfer coefficients were observed to be independent of the inclination angle despite changes in the prevailing flow patterns.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: International Journal of Multiphase Flow - Volume 80, April 2016, Pages 1–14
نویسندگان
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