Updated: February 27, 2001.
Copyright © 2001 by Walt W McNab, Concord, CA, U.S.A.. 
All Rights Reserved.

Computer-Mediated Distance Learning

Course on

 

MULTISPECIES REACTIVE TRANSPORT IN GROUNDWATER

INSTRUCTOR:

WALT W McNAB

 
Dr Walt McNab
Lawrence Livermore National Laboratory
Livermore, California, U.S.A.
 

TOPIC B: MODELING APPROACHES

 Lecture 4: Coupling of Geochemical and Transport Equations

 Introduction

Reactive transport simulation concerns the coupled solution of chemical reaction and solute transport equations. Throughout the previous lectures in this course, we have focused our attention on the relevant chemical reaction equations and looked at some of the techniques for solving them in batch systems (i.e., zero-dimensional domains without consideration of transport). In this lecture, we will see how multi-species solute transport can be coupled with solution of the chemical reaction equations to form a complete reactive transport modeling approach that will be used in the example problems of the subsequent lectures (Topic C).

 A mathematical overview

In systems in which there are multiple components existing within the aqueous phase, the advective-dispersive solute transport equation may be written for each component i:

(Eq.-1)

For our purposes in this course, we will assume that the groundwater velocity field is produced entirely in response to gradients in the potentiometric surface; that is, we are not considering density-driven flow. In systems with strong thermal or chemical concentration gradients, this assumption must be studied closely.

The source term for component i, G i, accounts for all of the different chemical processes that may affect the total concentration of i in the aqueous phase. As we have seen over the course of the lectures of Topic A, these processes include heterogeneous reactions ñ mineral dissolution and precipitation, adsorption, and ion exchange. The distribution of component i among various species in turn can be computed from mass balance, mass action, charge balance, and operational electron balance equations.

There are two general types of approaches for mathematically addressing the subject of coupling between the transport and chemistry equations. The one-step approach entails solving all of the equations for each component simultaneously, so that the advective-dispersive transport equation and all of the chemical equations are solved for one degree of freedom per component. Because cross terms exist in the chemical reaction equations (i.e., multiple components are included in many of the expressions), obtaining solutions by the one-step approach for systems of realistic complexity can be computationally very intensive. We will not be discussing the one step approach in this course.

An alternative approach, one that is used by most reactive transport models, is to de-couple the solutions to the transport and chemical reaction equations using the so-called two-step approach. In this case, the advective-dispersive transport equation is solved separately for each component over a relatively small time step. This is accomplished by discretizing the flow domain into small volume elements and replacing the partial differential equation for advective-dispersive transport (Eq.-1) by a difference equation using finite element or finite difference methods. These methods are discussed elsewhere in numerous textbooks on groundwater modeling as well as the a self-study computer mediated distance learning course offered by CMDL E&T, MODELING GROUND WATER FLOW AND CONTAMINANT TRANSPORT. Transport of solutes between the volume elements can produce water compositions that are out of chemical equilibrium, as happens, for example, when a water composition that is in equilibrium with one mineral assemblage in transported into a volume element characterized by a different mineral assemblage. Thus, a driving force exists to force new mass transfers within each volume element as a result of chemical reactions either coming into a new state of equilibrium or approaching such a state via kinetically-dominated reactions. Thus, the second step of the two-step approach entails solving the chemical reaction equations for each volume element in the system. The changes in total concentration for each component is noted and then included in the source term in the transport equation. The process is then repeated for the next time step. The overall strategy for the two-step approach is summarized in Figure 1.

Figure 1. The two-step approach to reactive transport modeling.

 An example

As has been our strategy in many of the prior lectures in this course, letís see how we can couple solute transport and chemical reactions using a simple example problem (with PHREEQC, of course). Consider a situation in which we have rainwater that is in equilibrium with the average CO2 present in the earthís atmosphere (partial pressure ~ 1 x 10-3 atm.). Now suppose this rainwater infiltrates a column of unweathered igneous rock consisting entirely of K-feldspar, KAlSi3O8, a major constituent of granitic rocks, at a pore velocity of 50 cm/yr.

 

Figure 2. Infiltration of acidic rainwater into a column of K-feldspar.

 

Keep in mind that CO2, when dissolved in water, forms a weak acid:

                                               (Eq.-2)

This acid may, in turn, facilitate the dissolution of K-feldspar,

      (Eq.-3)

The enrichment of the aqueous phase with the constituent species comprising may lead to saturation and precipitation of the weathering product kaolinite:

(Eq.-4)

Letís look at a 1-m long column, divided into 20 equal-size volume elements. Initially, at any point in the column, given a porosity of 0.20 (fractures), we can calculate that 0.004 m3 or K-feldspar exists for each kg of water, corresponding to roughly 39 moles (assuming a density of 2.7 g/cm3 and a molecular weight of 278 g/mole). Over time, as infiltrating rainwater passes through the rock, K-feldspar will convert to kaolinite, a familiar observation to geologists.

 

So how do we set up this problem in PHREEQC? Much of the problem definition involves key words we have already learned how to use in the past few lectures. We need now only learn how to break the system up into separate cells that define the column and specify how solutes and transferred between the cells. This is accomplished under the "TRANSPORT" key word.

Keep in mind that the number of cell shifts, multiplied by the number of cells, implies that PHREEQC will need to solve 1,000,000 separate batch chemistry models for this simulation. This may require up to an hour or more of CPU time, depending, of course, on the type of processor. This should serve as a first warning as to the perils of reactive transport modeling!

 

Here are some of the results of this simulation to ponder:

Table 1. Carbonate equilibria in rainwater and in column water in contact with K-feldspar.

Parameter

Influent rainwater

Native groundwater (1st cell, after 1000 years)

pH

5.41

9.42

CO2 (or H2CO3)

3.4 x 10-5

2.8 x 10-8

HCO3-

3.9 x 10-6

3.4 x 10-5

CO32-

4.7 x 10-11

4.4 x 10-6

 

Figure 3. Concentration profile of the Cl- tracer in the column after 1 year.

 

Figure 4. Amounts of K-feldspar and kaolinite present in the column after 5000 years.

Keep in mind that this particular example problem is highly idealized and contrived. In the real world, a system such as this would exhibit far more complex behavior because (1) a number of different mineral phases besides those specified here would be present, each serving to buffer pH, Al3+, H4SiO4, etc. in the aqueous phase, and (2) rates of mineral precipitation and dissolution throughout the column would reflect the influences of reaction kinetics, which were not simulated. Nevertheless, this example clearly illustrates a central, recurring concept of reactive transport in real hydrogeochemical systems: reaction fronts will almost always lag significantly behind the water movement front. The actual movement of infiltrating rainwater through the column, as delineated by the Cl- tracer, takes approximately 2 years (the agreement between the PHREEQC numerical model and the Ogata-Banks (1961) solution is excellent). However, only a small portion of K-feldspar has been replaced by kaolinite in the first cell of the simulated column by 5000 years. Extrapolating, the reaction front as delineated by the mineral phases would require some 240,000 years before it begins to resemble the water movement front at 1 year. The message here is clear: the relatively low solubilities of mineral phases, the large number of moles of mineral phases present per unit volume in comparison to aqueous concentrations, and low rates of groundwater movement imply that substantial mineral dissolution requires a very long time. And keep in mind that we find this to be true under equilibrium assumptions; employing reaction kinetics in our modeled systems will slow things down still further. We will find this issue raising its head again and again in forthcoming simulations in subsequent lectures.

 Your assignment

How would the results of this simple reactive transport demonstration change if the problem were made more realistic, perhaps by introducing other mineral phases? Try, for example, adding quartz ñ SiO2, muscovite ñ KAl3Si3O10(OH)2, and a finite amount of kaolinite as initial phases in the column along with K-feldspar, or try including gibbsite, Al(OH)3, as an additional weathering product (i.e., not initially present). What are the consequences? Can you explain some of the things that are happening?

You are now ready to continue to

TOPIC C: INTRODUCTION TO REACTIVE TRANSPORT MODELING WITH PHREEQC: EXAMPLE APPLICATIONS.

         LECTURE 1: Acid Mine Drainage.

You may e-mail me questions and comments.

Walt W. McNab
E-mail address: mcnab1@llnl.gov.

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