کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
651241 1457410 2015 14 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Early onset of flow separation with rarefied gas flowing in a 90° bend tube
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی جریان سیال و فرایندهای انتقال
پیش نمایش صفحه اول مقاله
Early onset of flow separation with rarefied gas flowing in a 90° bend tube
چکیده انگلیسی


• Flow separation at Re = 1 with rarefied gas flow through 90° bend.
• Three distinct flow zones with different flow behaviors near bend plane.
• Pressure drop larger with bend compared to straight; difference reduces in slip regime.
• Flow nearly isothermal.
• Considerably different flow behavior than that of continuum.

This paper presents experimental and three-dimensional numerical study of early onset of separation with rarefied gas flow through a tube with single sharp 90° bend. Experiments are conducted for nitrogen gas flowing at low pressures in three conventional size tubes. The flow is dynamically similar to gas flow in a microchannel as the Knudsen number range (0.0003 < Kn < 0.0385) covers part of the continuum and the slip flow regime while maintaining the Reynolds number between 0.27 and 418.5. The static pressures along the inner, outer and top walls are measured for different mass flow rates and analyzed to understand the flow behavior. The static pressure measurement indicates adverse pressure gradient near the bend along the inner and outer walls of the tube at much lower value of Reynolds number as compared to conventional flow. The numerical solution of the Navier–Stokes equations with the Maxwell’s slip boundary condition shows good agreement with experimental data and helps bring out the complex flow behavior near the bend. The adverse pressure gradient, velocity profile, flow streamlines and velocity vectors in the bend plane clearly indicates secondary flows near the bend at as low a Reynolds number as unity. The flow acceleration and the presence of secondary flows near the bend causes a larger pressure drop as compared with a straight tube. Empirical correlations for Poiseuille number and additional pressure drop coefficient are proposed as part of this work. It is noted that limited experimental data exists in the literature for such flows; these results should therefore help enhance the fundamental understanding of gas flow in microchannels with bend.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Experimental Thermal and Fluid Science - Volume 66, September 2015, Pages 221–234
نویسندگان
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