Study of cooling with solidification of a laminar thermodependent Herschel-Bulkley fluid flow in a convectively cooled annular duct

被引:0
作者
Youbi, Z [2 ]
Benaouda-Zouaoui, B
Nouar, C
机构
[1] ENSEM, UHP, INPL,LEMTA, CNRS,UMR 7563, F-54504 Vandoeuvre Les Nancy, France
[2] Univ Blida, Inst Aeronaut, Blida, Algeria
关键词
Nusselt Number; Axial Velocity; Thermal Field; Local Nusselt Number; Rheological Parameter;
D O I
10.1007/BF01272522
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
This article presents a numerical analysis of cooling with solidification for laminar Herschel-Bulkley fluid flow in an annular duct. The outer cylinder is subject to uniform cooling with the surrounding sink temperature below the freezing temperature of the fluid. The inner cylinder is considered adiabatic. It is assumed that all the physical properties of the fluid except the consistency K are constant. The K-T relation used is K = a exp (-bT). Under this cooling condition, the thermal entrance region consists of two parts. The first one is a liquid - solidification free zone. The second one corresponds to the region where the solidification grows inward along the annular duct. The problem is governed by nine independent dimensionless numbers. Here, we focus on the effect of the rheological parameters and the thermo-dependency of K on the dynamic and thermal Fields. The effects of the rheological parameters are analyzed through the flow behavior index n, and the relative dimension of the plug core flow ap(e). Concerning the K-T variation effects, they can be described by the Pearson number Pn. Numerical results are obtained for the liquid-solidification free length z(f), liquid-solid interface profile, pressure drop, axial velocity evolution, plug core dimension and local Nusselt number. They indicate how the effect of Pn depends on ap(e) and n.
引用
收藏
页码:15 / 29
页数:15
相关论文
共 15 条
[1]   A FINITE-ELEMENT METHOD FOR INCOMPRESSIBLE NON-NEWTONIAN FLOWS [J].
BERCOVIER, M ;
ENGELMAN, M .
JOURNAL OF COMPUTATIONAL PHYSICS, 1980, 36 (03) :313-326
[2]   CREEPING MOTION OF A SPHERE THROUGH A BINGHAM PLASTIC [J].
BERIS, AN ;
TSAMOPOULOS, JA ;
ARMSTRONG, RC ;
BROWN, RA .
JOURNAL OF FLUID MECHANICS, 1985, 158 (SEP) :219-244
[3]  
BYRON-BIRD R., 1983, REV CHEM ENG, V1, P1
[4]   LIQUID SOLIDIFICATION IN A CONVECTIVELY-COOLED PARALLEL-PLATE CHANNEL [J].
CHENG, KC ;
WONG, SL .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1977, 55 (02) :149-155
[5]  
Crank J., 1984, Free and Moving Boundary Problems
[6]   VISCOPLASTIC FLOW IN CENTERED ANNULI, PIPES, AND SLOTS [J].
FORDHAM, EJ ;
BITTLESTON, SH ;
TEHRANI, MA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (03) :517-524
[7]   EXPERIMENTAL-STUDY OF LAMINAR HEAT-TRANSFER TO IN-TUBE FLOW OF NON-NEWTONIAN FLUIDS [J].
JOSHI, SD ;
BERGLES, AE .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1980, 102 (03) :397-401
[8]  
KUZAY TM, 1979, AICHE S SERIES, V189, P95
[9]   NUMERICAL-ANALYSIS OF THE THERMAL-CONVECTION FOR HERSCHEL-BULKLEY FLUIDS [J].
NOUAR, C ;
LEBOUCHE, M ;
DEVIENNE, R ;
RIOU, C .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 1995, 16 (03) :223-232
[10]  
OCKENDON H, 1997, J FLUID MECH, V83, P177