Skip to main content
U.S. flag

An official website of the United States government

Here’s how you know

Dot gov

Official websites use .gov
A .gov website belongs to an official government organization in the United States.

HTTPS

Secure .gov websites use HTTPS
A lock (LockA locked padlock) or https:// means you have safely connected to the .gov website. Share sensitive information only on official, secure websites.

  • Environmental Topics
  • Laws & Regulations
  • Report a Violation
  • About EPA
Contact Us

Grantee Research Project Results

Final Report: A Hierarchical Modeling Framework for Geological Storage of Carbon Dioxide

EPA Grant Number: R834385
Title: A Hierarchical Modeling Framework for Geological Storage of Carbon Dioxide
Investigators: Celia, Michael A.
Institution: Princeton University
EPA Project Officer: Aja, Hayley
Project Period: December 1, 2009 through November 30, 2013
Project Amount: $870,009
RFA: Integrated Design, Modeling, and Monitoring of Geologic Sequestration of Anthropogenic Carbon Dioxide to Safeguard Sources of Drinking Water (2009) RFA Text |  Recipients Lists
Research Category: Drinking Water , Water

Objective:

The project had four general goals and objectives: (1) to develop and enhance a set of analytical and numerical computational tools for simulation of CO2 injection, migration, and possible leakage; (2) to develop a "hierarchical modeling framework" within which different computational tools can be combined to produce effective hybrid models; (3) to provide guidance on level of model complexity for different scenarios; and (4) to provide simple-to-use web-based interfaces for different versions of the codes we develop.

Summary/Accomplishments (Outputs/Outcomes):

Objectives 1 and 2:
 
These two objectives together involve development of new modeling approaches that provide efficient computational solutions for problems associated with CO2 injection, migration, and leakage. The overall idea is to develop a range of solution options, including numerical and analytical solutions, and to combine them in ways that are justifiable in terms of the system physics, and lead to simplified solution algorithms. We use assumptions of vertical equilibrium, based on the strong buoyancy in the system, in almost all of these models. Numerical models, in which large-scale heterogeneity can be incorporated, are used at the large scale – we refer to these as “coarse-scale” models. Within a grid cell of the coarse models, we use analytical solutions to represent local-scale behavior associated with features like wells and faults. When combined, these provide a “multi-scale” modeling framework that covers a hierarchy of scales.
 
Major developments under these objectives include the following:
  • We have developed a set of fairly general numerical models based on vertically integrated governing equations under the assumption of vertical equilibrium (VE). These models provide significant computational advantages because of the reduction of dimensionality (three dimensions (x,y,z) reduced to two dimensions (x,y)). We note that these models do not require an assumption of a macroscopic sharp interface separating the two fluids (CO2 and brine) – a capillary transition zone in the vertical direction, consistent with the local-scale capillary pressure-saturation relationship, fits naturally into these models. See Gasda et al. (2012) or Nordbotten and Celia (2012) for details. Our numerical models include all major processes relevant to the CO2 storage problem, and can accommodate arbitrary heterogeneities in the horizontal directions. Processes modeled include different kinds of leakage through the caprock, including concentrated leakage along old wells or faults, and diffuse leakage through caprock formations, all in the context of multiple aquifer and aquitard sequences. The diffuse leakage treatment can be found in Janzen (2010) and Bandilla et al. (2013), while the treatment of leakage along old wells and along faults can be found in Celia et al. (2011) and Kang et al. (2014). Our numerical models also include capillary trapping of the injected CO2 (see Gasda et al., 2012) and more recently, we have derived a more general treatment of hysteresis and shown how local-scale hysteresis in both capillary pressure and relative permeability can be incorporated into vertically integrated models (Doster et al., 2013, 2014). These models also include dissolution of CO2 into brine with subsequent convective mixing (Gasda et al., 2011). In the dissolution work, we use an upscaled representation of the convective mixing based on averaging of highly-resolved fine-scale simulations of the unstable mixing in the vertical; the results are reasonable given the overall scales involved in the problem. These large-scale numerical models have been applied to several realistic scenarios, including simulations of the Illinois Basin (Bandilla et al., 2012), the Basal Formation in the Alberta Basin (and adjacent basins) (Huang et al., 2014), and the Johanson formation under the North Sea (Gasda et al., 2012). As mentioned earlier, all of these models allow for a general capillary transition zone, thereby alleviating the assumption of a sharp interface separating the CO2 and brine. The models that include dissolution use an upscaled expression for convective mixing, based on detailed simulations at the fine scale. These models capture the essential behavior of the dissolution process while allowing us to maintain computational efficiencies.
  • We have enhanced and applied our analytical and semi-analytical models for CO2 injection and migration; these models also include leakage of both CO2 and brine along old wells. These analytical models require additional simplifying assumptions, including horizontal and homogeneous aquifers, but they provide very efficient simulations, orders of magnitude faster than analogous numerical models. This efficiency allows injection into systems with many geological layers (alternating aquifers and aquitards) and many potentially leaky wells to be simulated in a few minutes on a single-processor computer. The paper of Celia et al. (2011) shows a specific example of how large-scale injection into realistic formations that have many potentially leaky wells, and many geological layers in the vertical direction, can be simulated. A sedimentary sequence in the Alberta Basin was used to study potential leakage of both CO2 and brine along a set of old wells. Results indicate that leakage rates are likely to be relatively low, for both CO2 and brine. The study of Nogues et al. (2012) expanded the studies of Celia et al. (2011) to identify specific measures of well properties that would lead to acceptably low leakage rates. In that study, we developed practical guidance for how well leakage might be analyzed when specific maximum leakage targets are identified (for example, no more than 0.1% leakage after 50 years of injection). The results in that paper showed what kinds of statistics the effective permeability along old wells must satisfy in order to meet target leakage criteria. We note that the guidance provided in Nogues et al. can be coupled with the implied values for well permeabilities derived in Tao and Bryant (2014) to indicate an expected low probability of leakage along old wells. In addition, we have derived a new analytical solution to represent fluid behavior in the vicinity of a leaky fault (Kang et al., 2014). That work shows how the fault properties play an important role in the solution, and how in the vicinity of the fault vertical flow effects, which are included in the local-scale analytical solution, can be important for proper calculation of the leakage rates.
  • We expanded the use of our simplified computational models to study new paradigms in CO2 storage. We published two paper (Bandilla et al., 2012a,b) in which we examined the large-scale impacts of basin-wide injections into the Mt. Simon aquifer. The extensive overlap of the Areas of Review led to exploration of brine production as a method of pressure control. In Court et al. (2012c), we studied more carefully the idea of using brine extraction for the purpose of pressure control. This subsequently led us to consider the idea of CCS more broadly, consistent with the expanded idea of CCUS (carbon capture, utilization, and storage). In particular, we began to explore potential synergies between geothermal energy production and CO2 injection. The papers of Elliot et al. (2013) and Buscheck et al. (2012) examined a number of different aspects of this idea, where heat from the produced fluids was extracted for geothermal energy. The brine extraction provides the corollary benefit of pressure control as well as control of the CO2 plume extent, while the CO2 injection provides complementary pressure support for the geothermal production.
  • We have recently developed a new class of models that relaxes the vertical equilibrium (VE) assumption while still using a vertically integrated framework. This gives the computational advantages of reduced spatial dimensionality while allowing for dynamics of CO2 and brine flows in the vertical direction. This is as opposed to the assumption of vertical equilibrium where the CO2 is always above the brine (instantaneously) with the two segregated fluids in pressure equilibrium. The underlying ideas are presented in the recent paper of Guo et al. (2014). This concept follows from the idea that VE models can be understood in the broad context of multi-scale models – this is explained in the textbook of Nordbotten and Celia (2012). This new model, which includes vertical dynamics, provides a model of intermediate complexity, where much of the dynamics inherent in fully three-dimensional models can be captured while still maintaining significant computational reductions. We are in the process of studying the numerical properties of this approximation and identifying its limitations, in particular the ways in which both pressure and saturation need to be treated when we include heterogeneity in the vertical direction.
  • In terms of the idea of “hierarchical” models, we have achieved this objective through the broader framework of multi-scale modeling. The general idea of the multi-scale framework is presented in Nordbotten and Celia (2012), where vertically integrated models were analyzed by identifying the vertical dimension as the “fine scale” and the horizontal dimensions as the “coarse scale”. This framework provides significant insights into vertically integrated models, and led directly to the derivation of the new ‘dynamic’ model of Guo et al. (2014). In addition to this broad framework for vertically integrated models, we have also provided additional fine-scale representations where analytical solutions at the fine scale (now in the horizontal direction) are embedded into numerical solutions at the coarse scale. The overall idea is to use local-scale analytical or semi-analytical solutions to represent local features like leaky wells or leaky faults, in the context of large-scale numerical models. The use of these local analytical solutions, which define a fine scale in the (x,y) horizontal plane, avoids the need for fine numerical discretization around these local features. These kinds of local-scale corrections have been developed for both pressure and CO2 saturation profiles in the vicinity of an injection well (Janzen, 2010) and in the context of leakage into a fault (Kang et al., 2014). Both of these follow, broadly, from the earlier work of Nordbotten and Celia (2006a,b) on analytical solutions and on two-phase upconing around leaky wells. The recent work on faults, which was much more complicated than anticipated, requires inclusion of information about both the formation and the fault region – see the details in Kang et al. (2014). We believe that these analytical solutions, which are embedded into larger-scale numerical grid blocks in the (x,y) plane, provide a very flexible framework for enhanced multi-scale modeling for practical CO2 injection problems.
Objective 3:
 
We have studied the range of applicability of vertical equilibrium models as well as other aspects of our modeling approach including the use of a sharp interface to separate the CO2 and brine, and the inclusion of VE models into a multi-scale framework. The range of models used in CO2 simulations, and the length and time scales over which they are appropriate, were summarized in the paper by Celia and Nordbotten (2010), and subsequently expanded in the book of Nordbotten and Celia (2012). The paper of Court et al. (2012a) specifically analyzes the conditions under which we can reasonably assume vertical equilibrium (VE) as well as a macroscopic sharp interface. The VE assumption requires that the time required for the two fluids to segregate by buoyancy is small relative to the simulation times. This criterion depends on density differences, vertical permeability, and some details of the multi-phase fluid properties. The assumption of a sharp interface depends strongly on the functional form of the local capillary pressure function, which controls the thickness of the capillary transition zone. When that zone is sufficiently thin, the sharp interface model is appropriate. Both of these assumptions, and the associated requirements for them to be valid, are explained in detail in the Court et al. (2012a) paper. The results of this analysis led us to develop methods that would allow both of these assumptions to be relaxed without losing computational efficiencies: all of our numerical models now allow for a finite capillary transition zone, which is calculated directly from the local-scale capillary pressure – saturation relationship, while the new dynamic model of Guo et al. (2014) alleviates the vertical equilibrium assumption and therefore allows for temporal dynamics for the CO2 saturation profile to develop in the vertical direction. We believe both of these fill in a major gap in the complexity spectrum for CO2 modeling, while answering criticisms of the vertical equilibrium and sharp interface assumptions. We have also performed a systematic computational study in which a number of models were compared based on their ability to predict areas of review associated with hypothetical large-scale injections into the Basal Aquifer of Canada. This work is reported in Huang et al. (2014). In that study, the limitations of analytical models to provide large-scale information was made clear, while we also observed that the relatively local extent of the CO2 plumes, as compared to the overall pressure footprint, made single-phase numerical models reasonable choices for modeling large-scale areas of review.
 
Objective 4:
 
We continue to offer a publically available web interface where simple calculations for CO2 plume evolution and pressure response can be calculated and visualized. We also have a second option to analyze the behavior of a system with one injection well, one leaky well, and two aquifers separated by a caprock. This can give a very quick idea of what leakage along one well might look like, and how a secondary plume might form in the overlying aquifer. The web interface can be found at http://monty.princeton.edu/CO2interface/. We have also organized and participated in several workshops, including a workshop we organized in Princeton in December 2010 that focused on model complexity and the role that simplified models can play in CO2 storage problems. The workshop included academics, representatives from industry, and representatives from the EPA. Two days of lively discussions and presentations focused on how simple models can be developed that still capture the essential features of the underlying processes. There appeared to be general consensus among this international group that was summed up by one participant (from industry) who said that “ninety percent of our learning is achieved through simple models." This provided further motivation for us to pursue our overall strategy to develop models that are “as simple as possible, but not simpler." The two senior researchers on the project, Prof. Celia and Dr. Bandilla, attended the EPA STAR workshop in Washington in January 2013 to present our project and to interact with other PI’s as well as EPA personnel. Among other things, this led to productive discussions about how our approaches to CO2 modeling might be useful to analyze practical questions about hydraulic fracturing and shale gas, especially questions related to leakage of both gas and fracking fluids. This led to participation in two subsequent EPA-organized workshops on fracking, the potential leakage of fluids, and the impacts on water resources, all in the context of shale-gas systems.
 

Conclusions:

A summary of results has been provided in Section 1 of this report. Here we highlight the significance of the accomplishments achieved in this project:
 
1. We have developed simplified vertical equilibrium models that can simulate the flow of both brine and CO2, tracking both the phase saturations and phase pressures. These models incorporate all important large-scale processes, including finite capillary transition zones, capillary trapping of both CO2 and brine, dissolution of CO2 into brine and subsequent dynamic convective mixing, and leakage through the caprock including both diffuse leakage and leakage along concentrated pathways. The convective mixing uses an upscaled expression for mixing dynamics, and the concentrated leakage pathways include both leaky wells and faults. These models have been applied to realistic field-scale injections including simulations of injection into the Illinois Basin (Mt Simon formation), the Alberta Basin (Basal aquifer), and the Johanson Formation underlying the North Sea. One recent result of particular interest is the demonstration, for injection into the Basal Aquifer, than simple models provide good estimates for large-scale information such as estimated areas of review.
 
2. We have identified conditions under which the assumption of vertical equilibrium is appropriate, based on time-scale analysis associated with buoyant segregation in the vertical direction. We have also identified the conditions under which the sharp-interface assumption is appropriate, based on length-scale analysis associated with the capillary transition zone. We have also shown that when these assumptions are valid, there is excellent match between our models and full three-dimensional models like the industry standard Eclipse.
 
3. We have expanded our earlier semi-analytical models, which are designed to simulate large-scale injection systems in which there are many potentially leaky wells. Our results, under hypothetical but realistic conditions, show that leakage along old wells appears to be minimal and should be manageable. A more general analysis of the leakage system, based on hundreds of thousands of simulations (made possible by our very efficient simulation tools), provide guidance on the ranges of wellbore permeabilities that are required to achieve expected leakage rates. We note that when this latter result is coupled with recent work from the University of Texas, which provides estimates for wellbore permeabilities, the probability of leakage along old wells again appears to be low.
 
4. We have developed a new algorithm that uses the vertically integrated equations associated with vertical equilibrium but relaxes the actual assumption of vertical equilibrium. This is developed in the context of a multi-scale framework for the governing equations in the CO2 system. This method is promising but requires further testing. If successful, it will fill a significant gap in the spectrum of model complexity, between VE models and traditional full three-dimensional simulators.
 
5. We have expanded our studies to include active management of brine in injection formations, motivated in part by the need to control pressure buildup in the formation. Corollary benefits include reduction in potential leakage of both CO2 and brine, and possible beneficial uses of water and/or heat associated with the extracted brine.
 
6. We have begun to investigate how our models for CO2 migration and leakage might be applied to issues associated with hydraulic fracturing and unconventional oil and gas production. This is motivated by discussions we have had with EPA personnel, beginning with the EPA workshop in Washington held in January 2013 and continuing with discussions at two subsequent EPA workshops focusing on potential fluid leakage in fracking systems.
 
7. All of our results are described in publications that are available in the open literature. A list of publications resulting from this project is given below.

References:

  1. Nordbotten, J.M. and M.A. Celia, "Similarity Solutions for Fluid Injection into Confined Aquifers", Journal of Fluid Mechanics, 561, 307-327, 2006a.
  2. Nordbotten, J.M. and M.A. Celia, "An Improved Analytical Solution for Interface Upconing Around a Well", Water Resources Research, 42, W08433 (doi:10.1029/2005WR004738), 2006b.
  3. Nordbotten, J.M. and M.A. Celia, Geological Storage of CO2: Modeling Approaches for Large-scale Simulation, John Wiley and Sons, Hoboken, NJ, 235 pages, 2012.
  4. Tao, Q. and S.L. Bryant, “Well Permeability Estimation and CO2 Leakage Rates”, International Journal of Greenhouse Gas Control, 22, 77-87, 2014.


Journal Articles on this Report : 18 Displayed | Download in RIS Format

Publications Views
Other project views: All 25 publications 18 publications in selected types All 18 journal articles
Publications
Type Citation Project Document Sources
Journal Article Bandilla KW, Celia MA, Elliot TR, Person M, Ellet KM, Rupp JA, Gable C, Zhang Y. Modeling carbon sequestration in the Illinois Basin using a vertically-integrated approach. Computing and Visualization in Science 2012;15(1):39-51. R834385 (2012)
R834385 (Final)
  • Abstract: Springer-Abstract
    Exit
  • Journal Article Bandilla K, Celia M, Birkholzer J, Cihan A, Leister E. Multiphase Modeling of Geologic Carbon Sequestration in Saline Aquifers. GROUNDWATER 2015;53(3):362-377. R834385 (Final)
  • Abstract from PubMed
  • Full-text: Wiley - Full Text HTML
    Exit
  • Other: Wiley - Full Text PDF
    Exit
  • Journal Article Buscheck TA, Sun YW, Chen MJ, Hao Y, Wolery TJ, Bourcier WL, Court B, Celia MA, Friedmann SJ, Aines RD. Active CO2 reservoir management for carbon storage: analysis of operational strategies to relieve pressure buildup and improve injectivity. International Journal of Greenhouse Gas Control 2012;6:230-245. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text: ResearchGate-Abstract and Full Text PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ScienceDirect-PDF
    Exit
  • Journal Article Celia MA, Nordbotten JM, Court B, Dobossy M, Bachu S. Field-scale application of a semi-analytical model for estimation of CO2 and brine leakage along old wells. International Journal of Greenhouse Gas Control 2011;5(2):257-269. R834385 (2010)
    R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text: ResearchGate-Abstract and Full Text PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ScienceDIrect-PDF
    Exit
  • Journal Article Court B, Elliot TR, Dammel JA, Buscheck TA, Rohmer J, Celia MA. Promising synergies to address water, sequestration, legal, and public acceptance issues associated with large-scale implementation of CO2 sequestration. Mitigation and Adaptation Strategies for Global Change 2012;17(6):569-599. R834385 (2012)
    R834385 (Final)
  • Abstract: Springer-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Court B, Bandilla KW, Celia MA, Buscheck TA, Nordbotten JM, Dobossy M, Janzen A. Initial evaluation of advantageous synergies associated with simultaneous brine production and CO2 geological sequestration. International Journal of Greenhouse Gas Control 2012;8:90-100. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text from PubMed
    Exit
  • Full-text: ScienceDIrect-PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Court B, Bandilla KW, Celia MA, Janzen A, Dobossy M, Nordbotten JM. Applicability of vertical‐equilibrium and sharp‐interface assumptions in CO2 sequestration modeling. International Journal of Greenhouse Gas Control 2012;10:134-147. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text from PubMed
    Exit
  • Full-text: ScienceDirect-PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Doster F, Nordbotten JM, Celia MA. Hysteretic upscaled constitutive relationships for vertically integrated porous media flow. Computing and Visualization in Science 2012;15(4):147-161. R834385 (Final)
  • Full-text: ResearchGate-Abstract & PDF Access
    Exit
  • Abstract: Springer-Abstract
    Exit
  • Journal Article Doster F, Nordbotten JM, Celia MA. Impact of capillary hysteresis and trapping on vertically integrated models for CO2 storage. Advances in Water Resources 2013;62(Part C):465-474. R834385 (Final)
  • Full-text: ScienceDirect-HTML
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ScienceDirect-PDF
    Exit
  • Journal Article Elliot TR, Celia MA. Potential restrictions for CO2 sequestration sites due to shale and tight gas production. Environmental Science & Technology 2012;46(7):4223-4227. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Abstract from PubMed
  • Abstract: ES&T-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Elliot TR, Buscheck TA, Celia M. Active CO2 reservoir management for sustainable geothermal energy extraction and reduced leakage. Greenhouse Gases: Science and Technology 2013;3(1):50-65. R834385 (2012)
    R834385 (Final)
  • Abstract: Wiley-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Gasda SE, Nordbotten JM, Celia MA. Vertically-averaged approaches for CO2 migration with solubility trapping. Water Resources Research 2011;47(5):W05528. R834385 (2010)
    R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text from PubMed
    Exit
  • Full-text: Wiley Online-Full Text HTML
    Exit
  • Abstract: Wiley Online-Abstract
    Exit
  • Other: Wiley Online-PDF
    Exit
  • Journal Article Gasda SE, Nordbotten JM, Celia MA. Application of simplified models to CO2 migration and immobilization in large-scale geological systems. International Journal of Greenhouse Gas Control 2012;9:72-84. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text: ScienceDirect-PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ResearchGate-Abstract
    Exit
  • Journal Article Guo B, Bandilla KW, Doster F, Keilegavlen E, Celia MA. A vertically integrated model with vertical dynamics for CO2 storage. Water Resources Research 2014;50(8):6269-6284. R834385 (Final)
  • Abstract: Wiley Online-Abstract
    Exit
  • Journal Article Huang X, Bandilla KW, Celia MA, Bachu S. Basin-scale modeling of CO2 storage using models of varying complexity. International Journal of Greenhouse Gas Control 2014;20;73-86. R834385 (Final)
  • Full-text: ScienceDirect-Full Text HTML
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Other: ScienceDirect-PDF
    Exit
  • Journal Article Kang M, Nordbotten JM, Doster F, Celia MA. Analytical solutions for two-phase subsurface flow to a leaky fault considering vertical flow effects and fault properties. Water Resources Research 2014;50(4):3536-3552. R834385 (Final)
  • Abstract: Wiley Online-Abstract
    Exit
  • Journal Article Nogues JP, Court B, Dobossy M, Nordbotten JM, Celia MA. A methodology to estimate maximum probable leakage along old wells in a geological sequestration operation. International Journal of Greenhouse Gas Control 2012;7:39-47. R834385 (2011)
    R834385 (2012)
    R834385 (Final)
  • Full-text: ScienceDirect-PDF
    Exit
  • Abstract: ScienceDirect-Abstract
    Exit
  • Journal Article Siirla-Woodburn E, Maxwell R. A heterogeneity model comparison of highly resolved statistically anisotropic aquifers. ADVANCES IN WATER RESOURCES 2015;75:53-66. R834385 (Final)
  • Full-text: ScienceDirect - Full Text HTML
    Exit
  • Other: ScienceDirect - Full Text PDF
    Exit
  • Supplemental Keywords:

    multi-phase flow, porous media, model complexity, sharp-interface assumption, two-phase flow

    Progress and Final Reports:

    Original Abstract
  • 2010 Progress Report
  • 2011 Progress Report
  • 2012 Progress Report
  • Top of Page

    The perspectives, information and conclusions conveyed in research project abstracts, progress reports, final reports, journal abstracts and journal publications convey the viewpoints of the principal investigator and may not represent the views and policies of ORD and EPA. Conclusions drawn by the principal investigators have not been reviewed by the Agency.

    Project Research Results

    • 2012 Progress Report
    • 2011 Progress Report
    • 2010 Progress Report
    • Original Abstract
    25 publications for this project
    18 journal articles for this project

    Site Navigation

    • Grantee Research Project Results Home
    • Grantee Research Project Results Basic Search
    • Grantee Research Project Results Advanced Search
    • Grantee Research Project Results Fielded Search
    • Publication search
    • EPA Regional Search

    Related Information

    • Search Help
    • About our data collection
    • Research Grants
    • P3: Student Design Competition
    • Research Fellowships
    • Small Business Innovation Research (SBIR)
    Contact Us to ask a question, provide feedback, or report a problem.
    Last updated April 28, 2023
    United States Environmental Protection Agency

    Discover.

    • Accessibility
    • Budget & Performance
    • Contracting
    • EPA www Web Snapshot
    • Grants
    • No FEAR Act Data
    • Plain Writing
    • Privacy
    • Privacy and Security Notice

    Connect.

    • Data.gov
    • Inspector General
    • Jobs
    • Newsroom
    • Open Government
    • Regulations.gov
    • Subscribe
    • USA.gov
    • White House

    Ask.

    • Contact EPA
    • EPA Disclaimers
    • Hotlines
    • FOIA Requests
    • Frequent Questions

    Follow.