Numerical simulation of non-isothermal pressure-driven miscible channel flow with viscous heating

被引:16
作者
Sahu, K. C. [1 ]
Ding, H. [2 ]
Matar, O. K. [3 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Hyderabad, Andhra Pradesh, India
[2] Univ Calif Santa Barbara, Dept Chem Engn, Santa Barbara, CA 93106 USA
[3] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, London SW7 2AZ, England
基金
英国工程与自然科学研究理事会;
关键词
Isothermal flow; Viscous heating; Channel flow; Miscible flow; Stability; Interfacial flow; CORE-ANNULAR-FLOW; SPATIALLY DEVELOPING FLOWS; CONSTRICTED CIRCULAR TUBE; HELE-SHAW CELL; VISCOSITY STRATIFICATION; CAPILLARY TUBES; CONVECTIVE/ABSOLUTE INSTABILITY; GLOBAL INSTABILITIES; LINEAR-STABILITY; CORRUGATED TUBE;
D O I
10.1016/j.ces.2010.02.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We study the pressure-driven, non-isothermal miscible displacement of one fluid by another in a horizontal channel with viscous heating. We solve the continuity, Navier-Stokes, and energy conservation equations coupled to a convective-diffusion equation for the concentration of the more viscous fluid. The viscosity is assumed to depend on the concentration as well as the temperature, while density contrasts are neglected. Our transient numerical simulations demonstrate the development of 'roll-up' of the 'interface' separating the fluids and vortical structures whose intensity increases with the temperature of the invading fluid. This brings about fluid mixing and accelerates the displacement of the fluid originally occupying the channel. Increasing the level of viscous heating gives rise to high-temperature, low-viscosity near-wall regions. The increase in viscous heating retards the propagation of the invading fluid but accelerates the ultimate displacement of the resident fluid. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3260 / 3267
页数:8
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