Hyperbolic Homogenized Models for Thermal and Solutal Dispersion

We formulate a general theory, based on a Lyapunov--Schmidt expansion, for averaging thermal and solutal dispersion phenomena in multiphase reactors, with specific attention to the important Taylor mechanism due to transverse intraphase and interphase capacitance-weighted velocity gradients. We show that the classical Taylor dispersion phenomena are better described in terms of low dimensional models that are hyperbolic and contain an effective local time or length scale in place of the traditional Taylor dispersion coefficient. This description eliminates the use of an artificial exit boundary condition associated with parabolic homogenized equations as well as the classical upstream-feedback and infinite propagation speed anomalies. Our approach is also applicable for describing steady dispersion in the presence of reaction and thermal generation or consumption. For two-phase systems, maximum dispersion is found to exist at an optimum fraction $\epsilon _{f}$ of the lower-capacitance phase. For the disp...

[1]  Wave model for longitudinal dispersion: Analysis and applications , 1995 .

[2]  G. Taylor Dispersion of soluble matter in solvent flowing slowly through a tube , 1953, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[3]  A. E. Kronberg,et al.  Wave model for longitudinal dispersion , 1995 .

[4]  G. M.,et al.  Partial Differential Equations I , 2023, Applied Mathematical Sciences.

[5]  J. Michael Ramsey,et al.  Dispersion Sources for Compact Geometries on Microchips , 1998 .

[6]  Vemuri Balakotaiah,et al.  Low-dimensional models for describing mixing effects in laminar flow tubular reactors , 2002 .

[7]  D. Vortmeyer,et al.  Equivalence of one- and two-phase models for heat transfer processes in packed beds: one dimensional theory , 1974 .

[8]  P. V. Danckwerts Continuous flow systems. Distribution of residence times , 1995 .

[9]  R. Aris,et al.  On the dispersion of a solute by diffusion, convection and exchange between phases , 1959, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[10]  Hsueh-Chia Chang,et al.  A theory for fast‐igniting catalytic converters , 1995 .

[11]  V. Balakotaiah,et al.  Runaway limits for homogeneous and catalytic reactors , 1995 .

[12]  Vemuri Balakotaiah,et al.  Classification of steady-state and dynamic behavior of distributed reactor models , 1996 .

[13]  P. V. Danckwerts Continuous flow systems , 1953 .

[14]  Anthony J. Roberts,et al.  Boundary conditions for approximate differential equations , 1992, The Journal of the Australian Mathematical Society. Series B. Applied Mathematics.

[15]  John F. Brady,et al.  Dispersion in fixed beds , 1985, Journal of Fluid Mechanics.

[16]  R. Aris,et al.  Observations on fixed‐bed dispersion models: The role of the interstitial fluid , 1980 .

[17]  Anthony J. Roberts,et al.  The utility of an invariant manifold description of the evolution of a dynamical system , 1989 .

[18]  P. C. Chatwin,et al.  The approach to normality of the concentration distribution of a solute in a solvent flowing along a straight pipe , 1970, Journal of Fluid Mechanics.

[19]  Vemuri Balakotaiah,et al.  Effective models for packed-bed catalytic reactors , 1999 .

[20]  K. Westerterp,et al.  Wave model for longitudinal dispersion: Development of the model , 1995 .

[21]  D. D. Perlmutter,et al.  A unified treatment of the inlet boundary condition for dispersive flow models , 1976 .

[22]  A. Majda,et al.  SIMPLIFIED MODELS FOR TURBULENT DIFFUSION : THEORY, NUMERICAL MODELLING, AND PHYSICAL PHENOMENA , 1999 .

[23]  A. J. Roberts,et al.  A centre manifold description of containment dispersion in channels with varying flow properties , 1990 .

[24]  Vemuri Balakotaiah,et al.  Dispersion of chemical solutes in chromatographs and reactors , 1995, Philosophical Transactions of the Royal Society of London. Series A: Physical and Engineering Sciences.