Regular Article
An investigation of the effect of pore scale flow on average geochemical reaction rates using direct numerical simulation
Article first published online: 30 MAR 2012
DOI: 10.1029/2011WR011404
This paper is not subject to U.S. copyright. Published in 2012 by the American Geophysical Union
Additional Information
How to Cite
, , , and (2012), An investigation of the effect of pore scale flow on average geochemical reaction rates using direct numerical simulation, Water Resour. Res., 48, W03527, doi:10.1029/2011WR011404.
Publication History
- Issue published online: 30 MAR 2012
- Article first published online: 30 MAR 2012
- Manuscript Accepted: 17 FEB 2012
- Manuscript Revised: 10 FEB 2012
- Manuscript Received: 22 SEP 2011
Funded by
- U.S. Department of Energy. Grant Number: DE-AC02-05CH11231
Keywords:
- computational fluid dynamics;
- geochemical reaction rates;
- modeling;
- pore scale;
- reactive transport;
- upscaling
[1] The scale-dependence of geochemical reaction rates hinders their use in continuum scale models intended for the interpretation and prediction of chemical fate and transport in subsurface environments such as those considered for geologic sequestration of CO2. Processes that take place at the pore scale, especially those involving mass transport limitations to reactive surfaces, may contribute to the discrepancy commonly observed between laboratory-determined and continuum-scale or field rates. Here, the dependence of mineral dissolution rates on the pore structure of the porous media is investigated by means of pore scale modeling of flow and multicomponent reactive transport. The pore scale model is composed of high-performance simulation tools and algorithms for incompressible flow and conservative transport combined with a general-purpose multicomponent geochemical reaction code. The model performs direct numerical simulation of reactive transport based on an operator-splitting approach to coupling transport and reactions. The approach is validated with a Poiseuille flow single-pore experiment and verified with an equivalent 1-D continuum-scale model of a capillary tube packed with calcite spheres. Using the case of calcite dissolution as an example, the high-resolution model is used to demonstrate that nonuniformity in the flow field at the pore scale has the effect of decreasing the overall reactivity of the system, even when systems with identical reactive surface area are considered. The effect becomes more pronounced as the heterogeneity of the reactive grain packing increases, particularly where the flow slows sufficiently such that the solution approaches equilibrium locally and the average rate becomes transport-limited.

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