کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
687905 1460075 2016 13 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Influence of three-start spirally twisted tube combined with triple-channel twisted tape insert on heat transfer enhancement
ترجمه فارسی عنوان
تاثیر سه لوله پیچ خورده مارپیچ ترکیبی با نوار سه تایی کانال پیچ خورده در افزایش انتقال حرارت
کلمات کلیدی
انتقال گرما، لوله مبدل حرارتی، سه پیچ لوله پیچ خورده، نوار پیچ خورده سه کاناله، نوار پیچ خورده
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تکنولوژی و شیمی فرآیندی
چکیده انگلیسی


• Effects of twisted tube combined with twisted tape on heat transfer are performed.
• The twisted tubes fitted with tape in belly-to-neck and belly-to-belly forms are studied.
• The tape in belly-to-neck form at w/D = 0.34 possesses the highest thermal performance.

In the present article, heat transfer enhancement by three-start spirally twisted tube combination with triple-channel twisted tape is studied numerically using RNG k-ε turbulence model. Influences of the tape width ratio (w/D = 0.1, 0.25, 0.34 and 0.5) and tube/tape arrangement (belly-to-belly and belly-to-neck arrangements) are described. The numerical results of a twisted tube without tape and a circular plain tube are also given for comparison. The results are reported in terms of velocity field, temperature field, turbulent kinetic energy, local Nusselt number distribution, average Nusselt number, pressure loss and thermal performance factor. It is found that heat transfer and friction factor increase with tape width ratio. At a given tape width, the systems in belly-to-neck arrangement are more efficient for heat transfer enhancement than the ones in belly-to-belly arrangement. The three-start spirally twisted tubes with twisted tapes in belly-to-neck arrangement at w/D = 0.1, 0.25 and 0.34 give higher Nusselt numbers than the twisted tube without tape up to 1.2%, 21% and 36%, respectively. The twisted tubes with triple-channel twisted tape in belly-to-belly arrangement provide higher Nusselt numbers than the twisted tube without tape up to 1.23%, 6.7%, 10% and 17%, respectively. The superior heat transfer of the combined devices in belly-to-neck arrangement (especially at large w/D) is attributed to the stronger interaction between the swirling flows induced by the tubes and those induced by the tapes. Moreover, the systems in belly-to-neck arrangement cause lower friction loss than the ones in belly-to-belly arrangement. Thus, the systems in belly-to-neck arrangement yield higher thermal performance factors. Among the studied cases, the twisted tube combined with triple-channel twisted tape in belly-to-neck arrangement at w/D = 0.34 possesses the maximum thermal performance of 1.32 at Reynolds number of 5000.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 102, April 2016, Pages 117–129
نویسندگان
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