Laminar swirling slender pipe flows

被引:2
作者
Sauer, Vinicius M. [1 ]
Fachini, Fernando F. [2 ]
机构
[1] Calif State Univ, Dept Mech Engn, Northridge, CA 91330 USA
[2] Inst Nacl Pesquisas Espaciais, Grp Mecan Fluidos Reat, BR-12630000 Sao Paulo, Brazil
基金
巴西圣保罗研究基金会;
关键词
HEAT-TRANSFER; LIQUID FLOW; DECAY;
D O I
10.1063/5.0229626
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Swirling flows are extensively used to enhance mixing in chemical and physical processes. Although many fundamental studies involve decaying laminar swirls in circular ducts with constant area-for which several theoretical descriptions exist-converging and diverging pipe sections are often employed, demanding the extension of the analysis to swirling laminar flows in pipes with varying areas. This work analytically investigates axial swirl decay in laminar axisymmetric flows in converging and diverging pipes at moderate Reynolds numbers. The theoretical model extends the classical theory for laminar low swirling flows in straight pipes with impermeable walls to pipes with slowly varying areas. Inlet Reynolds number and converging/diverging angle effects are analyzed for incompressible axisymmetric laminar flows in slender pipes (lengths much greater than the radius). Results show that diverging pipes enhance the swirl decay rate, whereas converging systems have a weakening effect for flows with the same inlet Reynolds number. Conversely, increasing the inlet angle in converging flows decreases the decay rate, whereas larger diverging pipe inlet angles promote swirl decay. A simplified eigenvalue analysis shows that the relationship between the swirl decay lengths in diverging ( & ell;(d,div)), straight ( & ell;(d,st)), and converging ( & ell;(d,conv)) pipes is given by & ell;(d,div)<& ell;(d,st)<& ell;(d,conv) for flows with similar inlet Reynolds numbers. Comparisons with numerical simulations show that the model predictions are almost exact for nondimensional pipe lengths up to 5x10(-2) times the inlet Reynolds number. Approximating the axial velocity profile through a fully developed function representative of laminar flows with heat transfer through the walls shows that the narrower axial velocity profile in diverging flows increases viscous effects, enhancing the swirl decay rate. On the contrary, the flatter axial velocity profile in converging pipes further extends the decay length.
引用
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页数:18
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共 71 条
[41]  
Lewellen W. S., 1971, A review of confined vortex flows
[42]   A comprehensive review on passive heat transfer enhancements in pipe exchangers [J].
Liu, S. ;
Sakr, M. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 19 :64-81
[43]   Turbulent flow in converging nozzles, part one: boundary layer solution [J].
Maddahian, R. ;
Farhanieh, B. ;
Firoozabadi, B. .
APPLIED MATHEMATICS AND MECHANICS-ENGLISH EDITION, 2011, 32 (05) :645-662
[44]   THERMAL DISTRIBUTIONS IN JEFFERY-HAMEL FLOWS BETWEEN NONPARALLEL PLANE WALLS [J].
MILLSAPS, K ;
POHLHAUSEN, K .
JOURNAL OF THE AERONAUTICAL SCIENCES, 1953, 20 (03) :187-196
[45]   Hydrodynamics and heat transfer in swirling flows in channels with swirlers (analytical review) [J].
Mitrofanova, OV .
HIGH TEMPERATURE, 2003, 41 (04) :518-559
[46]   Boundary layer solution for the turbulent swirling decay flow through a fixed pipe: SBR at the inlet [J].
Najafi, AF ;
Saidi, MH ;
Sadeghipour, MS ;
Souhar, M .
INTERNATIONAL JOURNAL OF ENGINEERING SCIENCE, 2005, 43 (1-2) :107-120
[47]   Simulation of turbulent swirling flow in convergent nozzles [J].
Nouri-Borujerdi, A. ;
Kebriaee, A. .
SCIENTIA IRANICA, 2012, 19 (02) :258-265
[48]   AXIAL FLOW IN A VORTEX [J].
NUTTALL, JB .
NATURE, 1953, 172 (4378) :582-583
[49]   LAMINAR FORCED-CONVECTION IN CONVERGING OR DIVERGING PLANAR SYMMETRIC DUCTS [J].
OZISIK, MN ;
TREPP, C ;
EGOLF, H .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1982, 25 (10) :1477-1480
[50]   The approxiamte integration of the differential equation of laminar boundary layer [J].
Pohlhausen, K .
ZEITSCHRIFT FUR ANGEWANDTE MATHEMATIK UND MECHANIK, 1921, 1 :252-268