Laplace transform approach to the rigorous upscaling of the infinite adsorption rate reactive flow under dominant Peclet number through a pore

In this article, we undertake a rigorous derivation of the upscaled model for reactive flow through a narrow and long two-dimensional pore. The transported and diffused solute particles undergo the infinite adsorption rate reactions at the lateral tube boundary. At the inlet boundary we suppose Danckwerts’ boundary conditions. The transport and reaction parameters are such that we have dominant Peclet number. Our analysis uses the anisotropic singular perturbation technique, the small characteristic parameter ε being the ratio between the thickness and the longitudinal observation length. Our goal is to obtain error estimates for the approximation of the physical solution by the upscaled one. They are presented in the energy norm. They give the approximation error as a power of ε and guarantee the validity of the upscaled model. We use the Laplace transform in time to get better estimates than in our previous article [Mikelić, Rosier, Rigorous upscaling of the infinite adsorption rate reactive flow under dominant Peclet number through a pore, Ann Univ Ferrara Sez. VII Sci. Mat. 2007 53, 333–359] and to undertake the study of important Danckwerts' boundary conditions.

[1]  R. Aris A - * On the Dispersion of A Solute in A Fluid Flowing Through A Tube , 1999 .

[2]  H. Bhadeshia Diffusion , 1995, Theory of Transformations in Steels.

[3]  P. Knabner,et al.  An analysis of crystal dissolution fronts in flows through porous media , 1998 .

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

[5]  Roberto Mauri,et al.  Dispersion, convection, and reaction in porous media , 1991 .

[6]  Steve Rosencrans,et al.  Taylor Dispersion in Curved Channels , 1997, SIAM J. Appl. Math..

[7]  Peter Knabner,et al.  Travelling wave behaviour of crystal dissolution in porous media flow , 1997 .

[8]  Willi Jäger,et al.  Diffusion, convection, adsorption, and reaction of chemicals in porous media , 1991 .

[9]  V. S. Vladimirov,et al.  Equations of mathematical physics , 1972 .

[10]  Andro Mikelic,et al.  Rigorous Upscaling of the Reactive Flow through a Pore, under Dominant Peclet and Damkohler Numbers , 2006, SIAM J. Math. Anal..

[11]  R. Dautray,et al.  Analyse mathématique et calcul numérique pour les sciences et les techniques , 1984 .

[12]  Peter Knabner,et al.  An Analysis of Crystal Dissolution Fronts in Flows through Porous Media Part 2: Incompatible Boundar , 1996 .

[13]  J. Scheid,et al.  Dispersion , 2004, Encyclopedic Dictionary of Archaeology.

[14]  Iuliu Sorin Pop,et al.  Effective dispersion equations for reactive flows with dominant Péclet and Damkohler numbers , 2007 .

[15]  C. J. Duijn,et al.  Crystal dissolution and precipitation in porous media: Pore scale analysis , 2004 .

[16]  A. Cottenie Soil chemistry, B. Physico-chemical models , 1980 .

[17]  Vemuri Balakotaiah,et al.  Spatially Averaged Multi-Scale Models for Chemical Reactors , 2005 .

[18]  M. Primicerio,et al.  MODELING AND HOMOGENIZING A PROBLEM OF ABSORPTION/DESORPTION IN POROUS MEDIA , 2006 .

[19]  R. W. Cleary,et al.  Chapter 10: Movement of Solutes in Soil: Computer-Simulated and Laboratory Results , 1979 .

[20]  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.

[21]  Andrey L. Piatnitski,et al.  Averaging a transport equation with small diffusion and oscillating velocity , 2001 .

[22]  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.

[23]  Stephen Whitaker,et al.  Dispersion in pulsed systems—I: Heterogenous reaction and reversible adsorption in capillary tubes , 1983 .

[24]  Andro Mikelić,et al.  Rigorous upscaling of the infinite adsorption rate reactive flow under dominant Peclet number through a pore , 2007 .

[25]  Hyperbolic averaged models for describing dispersion effects in chromatographs and reactors , 2004 .

[26]  Grégoire Allaire,et al.  Homogenization of a convection–diffusion model with reaction in a porous medium , 2007 .

[27]  Jacob Rubinstein,et al.  Dispersion and convection in periodic porous media , 1986 .