Difference between revisions of "User:Jhurley/sandbox"

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The persistent release of residual contaminants from low hydraulic conductivity (low ''k'') zones prevents many chlorinated solvent sites from reaching groundwater cleanup goals. Low ''k'' aquifer settings limit the effectiveness of many conventional remediation technologies that rely on extraction, recirculation, or amendment delivery and distribution to achieve contact between the residual contaminants and the reagents, contact which is necessary for subsequent contaminant transformation or destruction. Alternative methods are needed to effectively distribute remedial amendments, to control contaminants leaving low ''k'' source zones, and to enhance natural attenuation processes. Two innovative remediation technologies for the treatment of chlorinated solvents and other contaminants in low ''k'' media are introduced, along with operational and performance results from recent field demonstrations.
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A Conceptual Site Model (CSM) is a collection of information about a contaminated site that integrates the available evidence regarding its hydrogeologic setting, contaminant sources, exposure pathways, potential receptors, and site history.  A CSM for a [[Wikipedia: Light non-aqueous phase liquid | Light Non-Aqueous Phase Liquid (LNAPL)]] site focuses on several key concepts:  the stage in the LNAPL site life cycle, LNAPL distribution in the subsurface and the resulting mobility of the LNAPL, LNAPL as a source of dissolved and vapor plumes, and the attenuation of LNAPL sources over time.
 
<div style="float:right;margin:0 0 2em 2em;">__TOC__</div>
 
<div style="float:right;margin:0 0 2em 2em;">__TOC__</div>
  
'''Related Article(s):'''
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'''Related Article(s)'''
* [[Bioremediation - Anaerobic | Anaerobic Bioremediation]]
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* [[LNAPL Remediation Technologies]]
* [[Chemical Oxidation (In Situ - ISCO) | In Situ Chemical Oxidation]]
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* [[NAPL Mobility]]
* [[Chemical Reduction (In Situ - ISCR) | In Situ Chemical Reduction]]
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* [[Natural Source Zone Depletion (NSZD)]]
  
'''CONTRIBUTOR(S): '''  
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'''CONTRIBUTOR(S):''' [[Dr. Charles Newell, P.E. | Charles Newell]]
* [[Stephen D. Richardson, Ph.D., PE]]
 
* [[Craig E. Divine, Ph.D., PG]]
 
  
 
'''Key Resource(s):'''
 
'''Key Resource(s):'''
* The Horizontal Reactive Media Treatment Well (HRX Well<sup>&reg;</sup>) for Passive In-Situ Remediation<ref name="Divine2018a">Divine, C. E., Roth, T, Crimi, M., DiMarco, A.C., Spurlin, M., Gillow, J., and Leone, G., 2018. The Horizontal Reactive Media Treatment Well (HRX Well<sup>&reg;</sup>) for Passive In-Situ Remediation. Groundwater Monitoring & Remediation, 38(1), pp. 56–65.  [https://doi.org/10.1111/gwmr.12252 DOI: 10.1111/gwmr.12252]</ref>
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* LNAPL Site Management: LCSM Evolution, Decision Process, and Remedial Technologies. LNAPL-3. ITRC.<ref name="LNAPL-3">Interstate Technology and Regulatory Council (ITRC), 2018. LNAPL Site Management: LCSM Evolution, Decision Process, and Remedial Technologies. LNAPL-3. ITRC, LNAPL Update Team, Washington, DC.  [https://lnapl-3.itrcweb.org LNAPL-3 Website]</ref>  
  
* The Horizontal Reactive Media Treatment Well (HRX Well<sup>&reg;</sup>) for Passive In Situ Remediation: Design, Implementation, and Sustainability Considerations<ref name="Divine2018">Divine, C.E., Wright, J., Wang, J., McDonough, J., Kladias, M., Crimi, M., Nzeribe, B.N., Devlin, J.F., Lubrecht, M., Ombalski, D., Hodge, B., Voscott, H., and Gerber, K., 2018. The Horizontal Reactive Media Treatment Well (HRX Well<sup>&reg;</sup>) for Passive In Situ Remediation: Design, Implementation, and Sustainability Considerations. Remediation, 28(4), pp. 5-16. [https://doi.org/10.1002/rem.21571 DOI: 10.1002/rem.21571]&nbsp;&nbsp; Also available from: [https://www.researchgate.net/publication/327487096_The_horizontal_reactive_media_treatment_well_HRX_WellR_for_passive_in_situ_remediation_Design_implementation_and_sustainability_considerations ResearchGate]</ref>
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* Managing Risk at LNAPL Sites - Frequently Asked Questions, 2nd Edition. API.<ref name="Sale2018"> Sale, T., Hopkins, H., and Kirkman, A., 2018. Managing Risk at LNAPL Sites - Frequently Asked Questions, 2nd Edition. American Petroleum Institute (API), Washington, DC. 72 pages. [https://www.api.org/oil-and-natural-gas/environment/clean-water/ground-water/lnapl/lnapl-faqs Free download from API.] [https://www.enviro.wiki/index.php?title=File:Sale-2018_LNAPL_FAQs_2nd_ed.pdf Report.pdf]</ref>
  
* New Application of A Geotechnical Technology to Remediate Low-Permeability Contaminated Media – Final Technical Report<ref name="Richardson2020">Richardson, S.D., Hart, D.M., Long, J.A., and Newell, C.J., 2020. New Application of A Geotechnical Technology to Remediate Low-Permeability Contaminated Media – Final Technical Report. ER-201627, Environmental Security Technology Certification Program (ESTCP). [https://www.serdp-estcp.org/Program-Areas/Environmental-Restoration/Contaminated-Groundwater/Persistent-Contamination/ER-201627/ Project Overview]</ref>
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==Life Cycle of LNAPL Sites==
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[[File:Newell1w2Fig1.png | thumb | Figure 1.  Early, Middle, and Late Stage LNAPL releases<ref name= "Sale2018"/>.  The key distinctions are the presence of continuous LNAPL that can be mobile and the amount of time that has elapsed for NSZD to remove LNAPL.]]
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A Conceptual Site Model (CSM) is a collection of information about a contaminated site that integrates the available evidence regarding its hydrogeologic setting, contaminant sources, exposure pathways, potential receptors, and site history (see ASTM E1689-95(2014)<ref name="ASTM2014a"> ASTM, 2014. Standard Guide for Developing Conceptual Site Models for Contaminated Sites. ASTM E1689-95(2014), ASTM International, West Conshohocken, PA. [https://doi.org/10.1520/E1689-95R14 DOI: 10.1520/E1689-95R14]  http://www.astm.org/cgi-bin/resolver.cgi?E1689</ref> and ASTM E2531-06(2014)<ref name="ASTM2014b"> ASTM, 2014. Standard Guide for Development of Conceptual Site Models and Remediation Strategies for Light Nonaqueous-Phase Liquids Released to the Subsurface. ASTM E2531-06(2014), ASTM International, West Conshohocken, PA. [https://doi.org/10.1520/E2531-06R14  DOI: 10.1520/E2531-06R14]  http://www.astm.org/cgi-bin/resolver.cgi?E2531</ref>).  When developing a CSM for an LNAPL site, it is important to understand that LNAPL releases evolve and change from what are referred to as Early Stage sites to Middle Stage and then to Late Stage sites<ref name="Sale2018"/> (Figure 1). 
  
==Introduction==
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An Early Stage site is characterized by the presence of a continuous LNAPL zone where a thick layer of LNAPL accumulation (also known as free product) is observed in monitoring wells. The continuous LNAPL zone (or LNAPL body) may be mobile at Early Stage sites, migrating into previously non-impacted areas. Removal of significant LNAPL mass by active pumping may be feasible at these sites. Early Stage sites are now relatively rare in the United States due to stringent environmental regulations enacted in the 1980s which emphasized preventing releases.
[[File:Richardson1w2Fig1.png | thumb | 400px | Figure 1. Examples of low ''k'' geology. Upper left: bay muds, Oakland, California; lower left: weathered siltstone, Denver, Colorado; right: tailings slimes, central New Mexico<ref name="Horst2019"/>.]]
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[[File:Newell1w2Fig2a.png |thumb|left|500px| Figure 2a. Time lapse conceptualization of the formation of an LNAPL body<ref name="ITRC2019"> Interstate Technology and Regulatory Council (ITRC), 2019. LNAPL Training: Connecting the Science to Managing Sites. Part 1: Understanding LNAPL Behavior in the Subsurface. ITRC, Washington, DC. [[Media: ITRC2019_LNAPLtrainingPart1.pdf | Slides.pdf]]</ref>.]]
[[File:Richardson1w2Fig2.png | thumb | 400px | Figure 2. Contaminant back diffusion (“Matrix Diffusion”) from low ''k'' zones<ref name="NRC2005">National Research Council, 2005. Contaminants in the Subsurface: Source Zone Assessment and Remediation. National Academies Press, Washington, DC, pp. 372. [https://doi.org/10.17226/11146 DOI: 10.17226/11146]&nbsp;&nbsp; [[Media: NRC2005.pdf | Book.pdf]]</ref>.]]
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[[File:Newell1w2Fig2b.png |thumb|left|500px| Figure 2b. Sand tank experiment of an LNAPL release<ref name="ITRC2019"/>.]]
A critical challenge preventing many chlorinated solvent sites from achieving groundwater cleanup goals is the long term release of residual contaminants from low hydraulic conductivity (low ''k'') zones such as silts, clays, glacial till, over-bank deposits, marine deposits, tailings “slimes”, saprolite and bedrock (see Figure 1)<ref name ="Horst2019">Horst, J., Divine, C., Schnobrich, M., Oesterreich, R., and Munholland, J., 2019. Groundwater Remediation in Low-Permeability Settings: The Evolving Spectrum of Proven and Potential. Groundwater Monitoring & Remediation, 39(1), pp. 11-19. [https://doi.org/10.1111/gwmr.12316 DOI: 10.1111/gwmr.12316]</ref><ref name ="Sale2008">Sale, T., C. Newell, H. Stroo, R. Hinchee, and Johnson, P., 2008. Frequently Asked Questions Regarding Management of Chlorinated Solvents in Soils and Groundwater. Environmental Security Technology Certification Program (ESTCP) Project ER-0530, 38 pp. [[Media:2008-Sale-Frequently_Asked_Questions_Regarding_Management_of_Chlorinated_Solvent_in_Soils_and_Groundwater.pdf  | Report.pdf]]&nbsp;&nbsp; [https://serdp-estcp.org/Program-Areas/Environmental-Restoration/Contaminated-Groundwater/Persistent-Contamination/ER-200530/(language)/eng-US Project overview]</ref>. Such sites may be dominated by matrix diffusion processes (see Figure 2) which can significantly prolong restoration and site management timeframes. Residual contaminants residing in low permeability zones slowly diffuse from the low ''k'' matrix back into higher permeability zones, becoming a persistent source that is very difficult to remediate. One of the side effects of matrix diffusion is concentration rebound after an ''in situ'' treatment is applied. This is commonly observed at sites treated with chemical oxidation<ref name="McGuire2006">McGuire, T.M., McDade, J.M., and Newell, C.J., 2006. Performance of DNAPL Source Depletion Technologies at 59 Chlorinated Solvent-Impacted Sites. Groundwater Monitoring & Remediation. Volume 26, Issue 1, pp. 73-84.  [https://doi.org/10.1111/j.1745-6592.2006.00054.x DOI: 10.1111/j.1745-6592.2006.00054.x]&nbsp;&nbsp; [https://www.provectusenvironmental.com/marketing/p-ox1/McGuire%20et%20al%202006.pdf  Free download.pdf]</ref><ref name="Krembs2010">Krembs, F., Siegrist, R., Crimi, M., Furrer, R., and Petri, B., 2010. ISCO for Groundwater Remediation: Analysis of Field Applications and Performance. Groundwater Monitoring & Remediation, 30(4), pp. 42-53.  [https://doi.org/10.1111/j.1745-6592.2010.01312.x DOI: 10.1111/j.1745-6592.2010.01312.x]</ref> and has the potential to occur at ''in situ'' bioremediation sites after the depletion of electron donors<ref name="Adamson2011">Adamson, D., McGuire, T., Newell, C., and Stroo, H., 2011. Sustained Treatment: Implications for Treatment Timescales Associated with Source-Depletion Technologies. Remediation, 21(2), pp. 27-50.  [https://doi.org/10.1002/rem.20280 DOI: 10.1002/rem.20280]</ref>.
 
  
Currently, there are limited remediation options available to treat residual contamination trapped in low ''k'' zones. Low ''k'' settings limit the applicability and effectiveness of conventional remediation technologies due to the constraint on fluid introduction and recovery. As such, methods relying on extraction, recirculation, or reagent delivery and distribution are often limited in their effectiveness. For the long lived, difficult to treat sites, innovative technologies are needed that will reliably address mass flux limitations of contaminants leaving low ''k'' source zones, and also increase the actual treatment of the contaminants leaving these low ''k'' zones by enhancing natural attenuation processes. Two innovative technologies investigated by ESTCP are summarized below.
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Many sites in the U.S. are now considered to be in the Middle Stage, where the LNAPL thickness in wells has been largely depleted by natural spreading of the LNAPL body, [[Natural Source Zone Depletion (NSZD)]], smearing of the water table, and/or active remediation, and where the LNAPL bodies are stable or shrinking<ref name="LNAPL-3"/><ref name="Sale2018"/> (Figure 1). Active pumping characteristically only recovers LNAPL at relatively low rates of under 100 gallons per acre per year at Middle Stage sites, but NSZD rates may be much higher, on the order of 100s to 1,000s of gallons per acre per year.  Middle Stage dissolved phase plumes, typically comprised of monoaromatics such as benzene, toluene, ethyl benzene, and xylenes, are stable or shrinking over time.
  
==“Grout Bomber”==
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Late Stage sites only have a sparse distribution of residual (trapped) LNAPL due to long-term NSZD and any active remediation that has been performed at the site. The potential risks to receptors are typically low at Late Stage sites due to relatively low concentrations of LNAPL constituents in the dissolved phase and/or vapor plumes.
===Technology Description===
 
[[File:Richardson1w2Fig3.png | thumb | left | 400px | Figure 3. a) Grout Bomber equipment; b) hopper for mixing and delivery of grout to the “stitcher”; and c) grout exiting the mandrel]]
 
[[File:Richardson1w2Fig4.png | thumb | left | 400px | Figure 4. Application of the Bomber technology for contaminated sites in low ''k'' materials.]]
 
[[File:Richardson1w2Fig5.png | thumb | left | 400px | Figure 5. Chlorinated ethene concentrations at well pair (CMT-1 and IS17MW04).]]
 
The geotechnical industry offers a variety of well-established techniques for quickly and efficiently accessing the subsurface for the purposes of ground stabilization, foundation rehabilitation, porewater drainage, and structural support. The speed and efficiency of these techniques can also be a major advantage for emplacement of remedial amendments into the subsurface. One promising approach is the Grout Bomber, a larger adaptation of conventional cement or compaction grouting techniques for subsurface stabilization. The technology uses an excavator equipped with specialized equipment (a “stitcher”) to quickly push a mandrel (3.5 in. diameter hollow cylindrical rod) into the subsurface and subsequently fill the hole and subsurface voids with cement grout (from bottom to top) using an in-line grout delivery system. The typical arrangement of the Grout Bomber technology includes the installation rig (excavator with the “stitcher” mast; see Figure 3a) and an on-site grout mixing and delivery unit consisting of mixing hopper, pumps, hosing, and power supply. Raw materials are loaded into the mixing hopper (see Figure 3b) where it is mixed to the appropriate consistency, then pumped to the Bomber rig at a rate of approximately 0.25 cubic feet per pump stroke. At the exit end of the Bomber mandrel (see Figure 3c), the grout flows in a continuous and uniform manner, allowing the columns to be emplaced with grout while the mandrel (which was pushed into the subsurface) is lifted to the surface.  Hundreds of closely spaced vertical grout columns can be installed per day using this technology.
 
  
For environmental applications, the Grout Bomber approach can be “repurposed” as a means to improve delivery of remediation amendments into contaminated treatment zones in low ''k'' materials. The remedial amendment (e.g., mixture of zero-valent iron (ZVI), sand, neat oil) can replace the grout and be directly placed into the subsurface from bottom to top (not injected into the surrounding formation), creating hundreds of reaction columns. The Bomber technology offers the following benefits:
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==LNAPL Body Formation==
* '''Reduces uncertainty: '''
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LNAPLs released from tanks, pits, pipelines, or other sources will percolate downwards under the influence of gravity through permeable pathways in the unsaturated zone (e.g., soil pore space, fractures, and macropores) depending on the volume and pressure head of the LNAPL release, until encountering an impermeable layer or the water table, causing the LNAPL body to spread laterally. The Interstate Technology and Regulatory Council (ITRC)<ref name="LNAPL-3"/> describes this downward movement toward the water table this way:
The Bomber technology circumvents the “delivery problem” associated with conventional injection-based remediation approaches, particularly in low ''k'' zones. The closely spaced nature of the reaction columns (2-3 ft spacing) reduces the diffusion lengths out of low ''k'' zones and also the uncertainty associated with amendment delivery because contaminants are always < 1 - 1.5 ft from an active treatment zone (see Figure 4).
 
  
* '''Rapid installation of reaction columns: '''
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<blockquote>''During the downward movement of LNAPL through the soil, the presence of confining layers, subsurface heterogeneities, or other preferential pathways may result in irregular and complex lateral spreading and/or perching of LNAPL before the water table is encountered. Once at the water table, the LNAPL will spread laterally in a radial fashion as well as penetrate vertically downward into the saturated zone, displacing water to some depth proportional to the driving force of the vertical LNAPL column (or LNAPL head). The vertical penetration of LNAPL into the saturated zone will continue to occur as long as the downward force produced by the LNAPL head or pressure from the LNAPL release exceeds the counteracting forces produced by the resistance of the soil matrix and the buoyancy resulting from the density difference between LNAPL and groundwater.''<ref name="LNAPL-3"/></blockquote>
The Grout Bomber can install 100+ reaction columns per day to depths of 40-50 ft below ground surface (bgs) to encourage contaminant degradation in source zones. Since the Grout Bomber is a direct push technique, it is better suited to silts and clays with blow counts < 35. Consolidated materials with higher blow counts will require additional equipment to pre-drill the columns prior to amendment emplacement. In general, this technology represents a much simpler, less intensive, and easier to install version of complete soil mixing.  
 
  
* '''Accommodates various amendment types: '''
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While the release at the surface is still active, the LNAPL body can expand until the LNAPL addition rate is equal to the NSZD depletion rate.  However, once the release at the surface is stopped, the expansion will stop relatively quickly, and the LNAPL body will stabilize.  Figure 2a shows a conceptual depiction of this release scenario and Figure 2b shows a sand tank experiment of an LNAPL release.  Because of the buoyancy effects, LNAPL releases that reach the water table will form LNAPL bodies that “like icebergs, are partially above and below the water table”.<ref name="Sale2018"/>
In one example<ref name="Richardson2020"/>, vertical reaction columns containing a mixture of ZVI, vegetable oil, sand and minor amounts of water were installed to a depth of 30 ft bgs in a low ''k'' treatment area consisting primarily of silts, sandy clays, and lean clays<ref name="Divine2018"/>.  The ZVI-sand-oil mixture was designed to have a similar consistency (or viscosity) to cement grout, thus requiring no major alterations to the existing Bomber equipment for the project.  Recommended practices to ensure uninterrupted flow of amendments to the Bomber mandrel include:
 
** Conduct simple pumping pilot studies with amendments of varying consistencies,
 
** Consult with a well trained pump operator, and
 
** Minimize the length of hosing between mixing hopper pump and Bomber mandrel.
 
  
* '''Cost effective source zone treatment: '''
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==Key Implications of the LNAPL Conceptual Site Model==
Estimated treatment costs associated with emplacement of amendments with the Grout Bomber are ~$35 per cubic yard of source zone treated (including contractor labor, equipment, and materials). This is generally less than the reported unit cost for ''in situ'' biodegradation ($20-$80/yd<sup>3</sup>) and significantly less than chemical oxidation ($125/yd<sup>3</sup>) and thermal remediation (median $200/yd<sup>3</sup>)<ref name="McDade2005">McDade, J.M., T.M. McGuire, and Newell, C.J., 2005. Analysis of DNAPL Source Depletion Costs at 36 Field Sites, Remediation, 15(2), pp. 9-18[https://doi.org/10.1002/rem.20039 DOI: 10.1002/rem.20039]</ref>.
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The nature of multi-phase flow processes in porous media (e.g., the interaction of LNAPL, water, and air in the pore spaces of an unconsolidated aquifer) has several important implications for environmental professionals in areas including interpretation of LNAPL thickness in monitoring wells and assessment of the long-term risk associated with LNAPL source zonesA few of the key implications are described below.
  
===Operational Approach & Results===
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===Three States of LNAPL===
A field demonstration was conducted at Site 17, Naval Support Facility Indian Head, Maryland. The treatment area consists primarily of silts, sandy clays, and lean clays with TCE concentrations in soil and groundwater of up to 250 mg/kg and 400 mg/L, respectively. Eight hundred reaction columns (consisting of ZVI/sand or oil/sand), were installed 2-3 ft apart, to a depth of 30 ft bgs at the site. Approximately 100 reaction columns were installed per day, with the most productive day totaling 180 columns. During operation, installation time for each reaction column was on the order of 1-2 minutes. Overall, 77,000 lbs of ZVI and 650 gallons of vegetable oil were emplaced within the source area of ~5,000 ft<sup>2</sup>.
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LNAPL can be found in the subsurface in three different states:
  
===Performance Results===
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# '''Residual LNAPL''' is trapped and immobile but can undergo composition and phase changes and generate dissolved hydrocarbon plumes in saturated zones and/or vapors in unsaturated zones. The fraction of the total pore space occupied by this discontinuous LNAPL is referred to as the residual saturation, with other phases such as water and air in the remainder of the pore space.
Ongoing post installation monitoring of treatment area groundwater has found moderate reductions in TCE in site monitoring wells and that key degradation products that serve as indicators for both abiotic and biotic mechanisms (i.e., acetylene, ethene/ethane) are present. Samples from Continuous Multilevel Tubing (CMT) wells installed within reaction columns (anulus filled with ZVI amendment) have demonstrated 1-3 orders of magnitude reductions in TCE relative to the surrounding formation water (see Figure 5). These results provide evidence that the reaction columns are creating steep concentration gradients that could drive contaminants out of low permeability zones. Further, gaseous products (e.g., propane, propene, i-butane, n-butane, n-pentane, n-hexane) were detected in the unsaturated zone of several reaction columns further supporting abiotic TCE degradation. Results of this full scale project were very promising and, although several operational improvements were identified (e.g., improved pumpability of ZVI/sand mixture; minor equipment modifications; improved site prep practices), the Bomber technology has the potential to be an important remediation alternative for hard-to-treat chlorinated source zones, particularly ones with large, persistent matrix diffusion sources over large areas.
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# '''Mobile LNAPL''' is LNAPL at greater than the residual saturation. Mobile LNAPL can accumulate in a well and is potentially recoverable, but is not migrating (i.e., the LNAPL body is not expanding).
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# '''Migrating LNAPL''' is LNAPL at greater than the residual concentration which is observed to expand into previously non-impacted locations over time (e.g., LNAPL appears in a monitoring well that had previously been clean).
  
==Horizontal Reactive Treatment Well (HRX Well<sup><small>&reg;</small></sup>)==
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These three LNAPL states can cause different concerns and in some cases require different remediation goals.  
{| class="wikitable" style="margin-left: auto; margin-right: 30px; float:left; text-align:center;"
 
|+ Table 1. Potential reactive media types and target groundwater contaminants for an HRX Well<sup>&reg;</sup>
 
|-
 
! Reactive Media !! Potential Target Groundwater Contaminants
 
|-
 
| Zero valent iron (ZVI)</br>Bimetallics (e.g., ZVI + Pd, Pt, or Ni) || Chlorinated solvents (CVOCs), nitrate, perchlorate, energetics, chromium, arsenic
 
|-
 
| Granulated activated carbon (GAC)</br>Organosilicates || CVOCs, Poly- and Perfluoroalkyl substances (PFASs), hydrocarbons, halomethanes
 
|-
 
| Sustained Release Oxidants || CVOCs, 1,4-dioxane, hydrocarbons,</br>polyaromatic hydrocarbons (PAHs), phenolic compounds
 
|-
 
| Biodegradable particulate organic carbon</br>(e.g., mulch) || CVOCs, nitrate, perchlorate, energetics
 
|-
 
| Ion exchange resins || PFAS, brines
 
|-
 
| Phosphates (e.g., apatite) || Lead, uranium, other metals and radionuclides
 
|-
 
| Limestone, lime, magnesium oxide || Low pH, acid rock drainage
 
|-
 
| Barium sulfate (barite) || Radium
 
|-
 
| Iron sulfide || Chromium, high pH
 
|-
 
| Zeolites || Ammonium, radionuclides, PFAS
 
|}
 
[[File:Richardson1w2Fig6.png | thumb | 400px | Figure 6.  Conceptual HRX Well design<ref name="Divine2018a"/>. Groundwater (blue flowlines) is passively focused and flows into the fully screened HRX Well where it is treated as it flows through reactive media before exiting back into the aquifer. The hot colors represent high contaminant concentrations and cool colors represent treated water.]]
 
[[File:Richardson1w2Fig7.png | thumb | 400px | Figure 7. HRX Well completion demonstrating the minimal surface footprint requirement.]]
 
  
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===LNAPL “Apparent Thickness” is a Poor Metric for Risk Management===
 +
[[File:Newell1w2Fig3.png |thumb|left|600px| Figure 3.  Five LNAPL Thickness Scenarios for five different physical settings<ref name="Sale2018"/>.]]
 +
[[File:Newell1w2Fig4.png |thumb|350px| Figure 4.  Apparent LNAPL thickness versus LNAPL transmissivity, showing no correlation<ref name="Hawthorne2015">Hawthorne, J.M., 2015.  Nationwide (USA) Statistical Analysis of LNAPL Transmissivity, in: R. Darlington and A.C. Barton (Chairs), Bioremediation and Sustainable Environmental Technologies—2015. Third International Symposium on Bioremediation and Sustainable Environmental Technologies (Miami, FL), page C-017, Battelle Memorial Institute, Columbus, OH.  www.battelle.org/biosymp  [[Media:Hawthorne2015.pdf | Abstract.pdf]]</ref>.]]
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LNAPL thickness in monitoring wells is often referred to as the “apparent LNAPL thickness” because at first glance this LNAPL thickness might be expected to be the thickness of LNAPL that is in the formation, but in reality it is not well correlated with the thickness of the LNAPL zone in the subsurface for several reasons.
  
The Horizontal Reactive Media Treatment Well (HRX Well<sup>&reg;</sup>)<ref name="Divine2013"> Divine, C.E., Leone, G., Gillow, J, Roth, T., Brenton, H., and Spurlin, M., 2013. Horizontal In-well Treatment System and Source Area Bypass System and Method for Groundwater Remediation. U.S. Patent US8596351 B2. U.S. Patents and Trademarks Office, Alexandria, VA.    [[Media: HRXwellPatent.pdf  Patent.pdf ]]</ref><ref name="Divine2018a"/><ref name="Divine2018"/> is a new passive flux-control technology that utilizes large diameter horizontal wells filled with solid phase reactive media to treat contaminated groundwater ''in situ''The HRX Well is installed parallel to the direction of groundwater flow and the design leverages natural “flow focusing” behavior induced by the engineered contrast in hydraulic conductivity between the reactive media and the ambient aquifer hydraulic conductivity to passively capture and treat proportionally large volumes of groundwater within the well. Treated groundwater then exits the horizontal well along its down-gradient sections (Figure 6). The HRX Well can quickly reduce contaminant mass flux and control migration, however it will not directly treat source mass or contamination located in low permeability zones. It requires a limited above-ground footprint (Figure 7) and can be installed under buildings or other surface infrastructureIn involves no active groundwater management or above ground treatment systems, and minimal ongoing maintenance (except for periodic media replacement as the media becomes exhausted). As shown in Table 1, many different types of solid reactive media are already available; therefore, this concept could be used to address a wide range of contaminantsNote that it is anticipated that solid phase media would be used in most applications, however, other media types or treatment processes could conceivably be employed. It is expected that reactive media use would be more efficient, and its eventual replacement would be simpler and less costly for an HRX Well than for a conventional [[Zerovalent Iron Permeable Reactive Barriers | Permeable Reactive Barrier (PRB)]].
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First, different physical settings can produce different LNAPL thicknesses in monitoring wells. Sale et al. (2018) show five different scenarios that produce very different responses with regard to apparent LNAPL thickness (Figure 3). Scenario A shows an LNAPL apparent thickness in the monitoring well that is at static equilibrium with LNAPL in an unconfined aquifer. Scenario B, while also an unconfined aquifer, is comprised of very fine-grained soils that cause the LNAPL thickness in the well to be much higher than in Scenario AIn Scenario C, the LNAPL has accumulated under a confined unit (likely due to an underground release of LNAPL below the confining unit), and the LNAPL has risen above the groundwater potentiometric surface, leading to a large (and misleading) LNAPL thickness in the monitoring wellScenario D, LNAPL in a perched unit, also shows a very different response from the other scenariosScenario E, LNAPL in fractured system, shows that the LNAPL can penetrate below the water table, and that LNAPL thickness in a well is dependent on the pressure from accumulation of LNAPL in the fractures<ref name="Sale2018"/>.
  
For relatively thin aquifers, the vertically averaged capture and treatment zone width (''w<sub><small>ave</small></sub>'') for an individual well can be estimated through a simple manipulation of Darcy’s Law<ref name="Divine2018a"/>:
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Second, apparent LNAPL thickness is affected by changes in the groundwater surface elevation (or water table). Generally, when groundwater elevations are higher than typical, the LNAPL thickness in monitoring wells will decrease or go to zero because the groundwater will redistribute any mobile LNAPL into what previously was the unsaturated zone.  During lower groundwater elevation periods, much more of the LNAPL will occur as a continuous phase near the water table, leading to higher LNAPL thicknesses in wells.
::{|
 
| Equation 1.&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp; ||'''''<big>w'''<sub><small>ave</small></sub>''' = <sup>(K<sub><small>HRX</small></sub> &pi; r<sub><small>HRX</small></sub><sup>2</sup> i<sub><small>HRX</small></sub>)</sup> &frasl; <sub>(K<sub><small>A</small></sub> b<sub><small>A</small></sub> i<sub><small>A</small></sub>)</sub></big>'''''
 
|-
 
| Where:&nbsp;&nbsp;&nbsp;&nbsp;
 
|-
 
| ''K<sub><small>HRX</small></sub>'' || is the hydraulic conductivity of the treatment media,
 
|-
 
| ''r<sub><small>HRX</small></sub>'' || is the radius of the HRX Well,
 
|-
 
| ''i<sub><small>HRX</small></sub>'' || is the hydraulic gradient along the HRX Well,
 
|-
 
| ''K<sub><small>A</small></sub>'' || is the average hydraulic conductivity of the aquifer,
 
|-
 
| ''b<sub><small>A</small></sub>'' || is the targeted aquifer zone thickness, and
 
|-
 
| ''i<sub><small>A</small></sub>'' || is the ambient aquifer hydraulic gradient.   
 
|}
 
In all cases, ''i<sub><small>HRX</small></sub>'' < ''i<sub><small>A</small></sub>'', but for short wells, ''i<sub><small>HRX</small></sub>'' << ''i<sub><small>A</small></sub>'', and ''w<sub><small>ave</small></sub>'' is small. However, for long wells (several hundred feet or more), the difference between the hydraulic gradients diminishes. When used as a screening calculation, ''i<sub><small>HRX</small></sub>'' and ''i<sub><small>A</small></sub>'' can be assumed to be approximately equal in many cases. By inspection of Equation 1, it is clear that ''w<sub><small>ave</small></sub>'' increases as the permeability contrast between the aquifer and reactive media increases, and therefore this approach may be practical and cost effective for many moderate and lower permeability sites.  If necessary, multiple HRX Wells can be installed side by side to achieve target treatment widths. 
 
  
{| style="float:left; margin-left:auto; margin-right:30px;
+
Overall, LNAPL thickness measurements are useful for delineating the extent of mobile LNAPL in the saturated zone and can provide useful data for understanding the vertical distribution of LNAPL in the formation<ref name="Hawthorne2011">Hawthorne, J.M., 2011. Diagnostic Gauge Plots—Simple Yet Powerful LCSM Tools. Applied NAPL Science Review (ANSR), 1(2). [http://naplansr.com/diagnostic-gauge-plots-volume-1-issue-2-february-2011/ Website] [[Media:Hawthorne2011.pdf | Report.pdf]]</ref><ref name="Kirkman2013">Kirkman, A.J., Adamski, M., and Hawthorne, M., 2013. Identification and Assessment of Confined and Perched LNAPL Conditions. Groundwater Monitoring and Remediation, 33 (1), pp. 75–86. [https://doi.org/10.1111/j.1745-6592.2012.01412.x DOI:10.1111/j.1745-6592.2012.01412.x]</ref>. But LNAPL thickness by itself is a very poor indicator of the feasibility of LNAPL recovery<ref name="LNAPL-2">Interstate Technology and Regulatory Council (ITRC), 2009. Evaluating LNAPL Remedial Technologies for Achieving Project Goals. LNAPL-2. ITRC, LNAPLs Team, Washington, DC. www.itrcweb.org [[Media:ITRC-LNAPL-2.pdf | Report.pdf]]</ref><ref name="Hawthorne2015"/> (see [[NAPL Mobility]]) (Figure 4).  Because there is little correlation between apparent LNAPL thickness and LNAPL mobility, there is also little correlation between apparent thickness and the risk to receptors from the LNAPL.
| [[File:Richardson1w2Fig8.png | thumb | 480px | Figure 8.  Changes in groundwater flow characteristics before and after HRX Well installation showing the hydraulic effects of water discharging from the outlet screen. Posted and contoured values are groundwater elevations in feet above mean sea level.]]
 
| [[File:Richardson1w2Fig9.png | thumb | 400px | Figure 9. HRX Well installed at VAFB showing groundwater inflow (blue curved lines) and approximate outlet zone (shaded blue cone). Posted values represent reductions in TCE concentrations observed 436 days after HRX Well installation.]]
 
|}
 
The HRX Well concept has been evaluated with numerical models and physical sand tank experiments<ref name="Divine2018a"/><ref name="Divine2018"/>, and the first field scale installation of this technology was completed in August 2018 at Vandenberg Air Force Base (VAFB) in Central California. This purpose of the HRX Well is to control trichloroethene (TCE) flux in a thin (7 to 12 ft) low permeability aquifer (average hydraulic conductivity is approximately 0.1 to 0.5 ft/day) impacted at concentrations up to about 30 to 50 milligrams per liter (mg/L)The HRX Well consists of 85 ft of inlet screen and 70 ft of outlet screen separated by 165 ft of casing, with removeable treatment media cartridges (35 percent ZVI by weight, media hydraulic conductivity is approximately 100 ft/d) installed in 70 ft of the cased sectionHydraulic performance data (as shown in Figure 8) and treatment effectiveness data (Figure 9) indicate the following:
 
* The capture and treatment zone for this single HRX Well exceeded 50 ft, consistent with estimates predicted by Equation 1.
 
* TCE concentrations were reduced by more than 99.99% based on concentrations at the HRX Well outlet.
 
* Initial treatment response was observed in nearby monitoring wells generally within 150 days after HRX Well installation, which is consistent with the design model.
 
* 436 days after HRX Well installation, the TCE concentration in treatment wells was reduced by an average of 63%.  
 
  
For this site, the HRX Well concept compared favorably in terms of sustainability, relative to pump and treat (P&T) and conventional trench based PRB approaches.  The system operates passively ''in situ'', therefore, the recurring and cumulative energy requirements, carbon footprint, life cycle water consumption, recurring material use, and waste generation are low, and are primarily associated with replacement of treatment mediaFor the VAFB site, ZVI is contained in removable cartridges that are anticipated to require replacement every five to 10 yearsHowever, media replacement frequency is site specific and a function of contaminant loading and treatment media volume and characteristics. Lifecycle cost estimates for full-scale 30-yr systems also compared favorably: $2.5M to $3.1M for a three well HRX Well system, $3.8M to $4.7M for a P&T system, and $3.6M to $4.5M for a PRB design.  
+
===Complete LNAPL Remediation Is Very Challenging===
 +
Sale et al. (2018) described the problems with attaining complete LNAPL remediation this way:
 +
 
 +
<blockquote>''Experience of the last few decades has taught us: 1) our best efforts often leave some LNAPL in place, and 2) the remaining LNAPL often sustains exceedances of drinking water standards in release areas for extended periods. Entrapment of LNAPLs at residual saturations is a primary factor constraining our success. Other challenges include the low solubility of LNAPL, the complexity of the subsurface geologic environment, access limitations associated with surface structures, and concentration goals that are often three to five orders of magnitude less than typical initial concentrations within LNAPL zones.''<ref name="Sale2018"/></blockquote>
 +
 
 +
In particular, the discontinuous residual LNAPL cannot be removed (or recovered) by pumping, and ''in situ'' remediation is expensive and not completely effective (see [[LNAPL Remediation Technologies]]).  However, many regulatory programs require “LNAPL recovery to the extent practicable.”  The lack of quantitative metrics and the lack of correlation between apparent LNAPL thicknesses and subsurface LNAPL makes this a problematic requirement in many cases and the ITRC (2018) cautions “Thickness or concentration data alone may not provide a sound basis for defining the point at which a cleanup objective is achieved.”<ref name="LNAPL-3"/>  However, Sale et al. (2018) describe metrics such as LNAPL transmissivity, limited/infrequent well thicknesses, decline curve analysis, asymptotic analysis, and comparison to NSZD rates that can be used to determine when LNAPL has been removed the extent practicable<ref name="Sale2018"/>.
 +
 
 +
===Attenuation Processes are Active and Important===
 +
Both LNAPL source zones and their dissolved phase hydrocarbon plumes are attenuated by biodegradation and other attenuation process.  In the source zone, this attenuation is called [[Natural Source Zone Depletion (NSZD)]] (see also [[Natural Attenuation in Source Zone and Groundwater Plume - Bemidji Crude Oil Spill]]).  In the dissolved plume it is called [[Monitored Natural Attenuation (MNA)]] (see also  [[Biodegradation - Hydrocarbons]]).  These processes generally limit the length of dissolved phase hydrocarbon plumes to a few hundred feet<ref name="Newell1998">Newell, C.J., and Connor, J.A., 1998. Characteristics of Dissolved Hydrocarbon Plumes: Results from Four Studies, Version 1.1. American Petroleum Institute, Soil/Groundwater Technical Task Force, Washington, DC. [https://www.enviro.wiki/index.php?title=File:Newell-1998-chararacterization_of_dissolved_Pet._Hydro_Plumes.pdf Report.pdf]</ref> via processes that have been well known and understood since the mid-1990s.
 +
 
 +
However, NSZD is “by far, the biggest new idea for LNAPLs in the last decade.”<ref name="Sale2018"/>  Originally, LNAPL bodies were thought to attenuate very slowly via dissolution and volatilization.  In 2006, it was discovered that NSZD rates are orders of magnitude higher than originally thought, largely due to direct biodegradation of LNAPL constituents to methane and carbon dioxide by methanogenic consortiums of naturally occurring bacteria<ref name="Lundegard2006">Lundegard, P.D., and Johnson, P.C., 2006. Source Zone Natural Attenuation at Petroleum Spill Sites—II: Application to a Former Oil Field. Groundwater Monitoring and Remediation. 26(4), pp. 93-106.  [ https://doi.org/10.1111/j.1745-6592.2006.00115.x  DOI: 10.1111/j.1745-6592.2006.00115.x]</ref><ref name="Garg2017">Garg, S., Newell, C., Kulkarni, P., King, D., Adamson, D.T., Irianni Renno, M., and Sale, T., 2017. Overview of Natural Source Zone Depletion: Processes, Controlling Factors, and Composition Change. Groundwater Monitoring and Remediation, 37(3), pp. 62-81.  [https://doi.org/10.1111/gwmr.12219 DOI: 10.1111/gwmr.12219] [[Media:Garg2017gwmr.12219.pdf | Report.pdf]]</ref>.  NSZD processes play an important role in risk mitigation and the long-term stability of LNAPL bodies<ref name="Mahler2012">
 +
Mahler, N., Sale, T., and Lyverse, M., 2012. A Mass Balance Approach to Resolving LNAPL Stability. Groundwater, 50(6), pp 861-871.  [https://doi.org/10.1111/j.1745-6584.2012.00949.x DOI: 10.1111/j.1745-6584.2012.00949.x]</ref><ref name="LNAPL-3"/>.
 +
 
 +
===Risk from LNAPL Source Zones Diminishes Over Time===
 +
At Early Stage LNAPL sites, the expansion of the LNAPL body is a risk that needs to be addressed.  Fortunately, this type of site is relatively rare.  For Middle and Late Stage sites, the primary risks are associated with phase changes (dissolution of the LNAPL forming a dissolved plume and volatilization from the LNAPL or dissolved plume forming hydrocarbon vapors).  As described above, MNA can often control the dissolved phase (see [[Monitored Natural Attenuation (MNA) of Fuels]]), while aerobic biodegradation in the unsaturated zone greatly reduces the vapor intrusion risk from hydrocarbon vapors (see [[Vapor Intrusion - Separation Distances from Petroleum Sources]]).
 +
 
 +
Understanding LNAPL body mobility and stability is important to understand the potential risks posed by LNAPL.  The relative magnitude of LNAPL mobility can be determined by measuring the LNAPL transmissivity (see [[NAPL Mobility]]).  If the transmissivity is below a threshold level (in the range of 0.1 to 0.8 ft2/day) then the LNAPL likely cannot be recovered efficiently by pumping, but above this transmissivity level recovery is feasible<ref name="LNAPL-3"/>.  Michigan’s LNAPL guidance states “if the NAPL has a transmissivity greater than 0.5 ft2/day, it is likely that the NAPL can be recovered in a cost-effective and efficient manner unless a demonstration is made to show otherwise.”  Kansas LNAPL guidance requires “recovery of all LNAPL with a transmissivity greater than 0.8 ft2/day that can be recovered in an efficient, cost-effective manner.”<ref name="LNAPL-3"/>.  The stability of the entire LNAPL body can be evaluated using statistical tools to determine if migration of LNAPL is occurring<ref name="Hawthorne2013">Hawthorne, J.M., Stone, C.D., Helsel, D., 2013. LNAPL Body Stability Part 2: Daughter Plume Stability via Spatial Moments Analysis. Applied NAPL Science Review (ANSR), 3(5).  [http://naplansr.com/lnapl-body-stability-part-2-daughter-plume-stability-via-spatial-moments-analysis-volume-3-issue-5-september-2013/ Website] [[Media:Hawthorne2013.pdf | Report.pdf]]</ref>.
 +
 
 +
==Overview of Modern LNAPL Conceptual Site Model==
 +
[[File:Newell1w2Fig5.png |thumb|500px| Figure 5.  A higher tier of LNAPL CSM is useful as LNAPL site complexity increases<ref name="LNAPL-3"/>.]]
 +
The ITRC (2018) describes the typical evolution of an LCSM over the course of the remediation process which can be broken into three separate stages:
 +
* An ''Initial LCSM'' focuses on identifying the LNAPL concerns, such as a risk to health or safety, any LNAPL migration, LNAPL-specific regulations, and physical or aesthetic impacts.
 +
* A ''Remedy Selection LCSM'' supports remedial technology evaluation by characterizing aspects of the LNAPL and site subsurface that may impact remedial technology performance.
 +
* A ''Design and Performance LCSM'' focuses on presenting the technical information needed to establish remediation objectives, design and implement remedies or control measures, and track progress toward defined remediation endpoints.
 +
 
 +
One key question when developing an LCSM is “how much data is enough.”  In general, the answer is that the existing data is sufficient for the current stage of the remediation project when it allows the stakeholders to agree on a path forward<ref name="LNAPL-3"/>. Figure 5 shows that as the level of complexity of a site increases, a higher tier of LCSM is useful to provide enough information for making decisions<ref name="LNAPL-3"/><ref name="ASTM2014a"/>. The higher tier of information could be higher data density, additional tools for a given line of evidence, or other evaluations.
 +
 
 +
==LNAPL Concerns, Remediation Goals and Objectives==
 +
Finally, the ITRC (2018) provides a methodology for identifying LNAPL concerns, verifying those concerns, selecting LNAPL remediation goals, and determining LNAPL remediation objectives.  Examples of each of these concepts are provided below:
 +
 
 +
* '''Potential Concerns:'''  Human or ecological risk concerns, fire or explosivity issues, LNAPL migration, LNAPL-specific regulatory concerns, other concerns such as odors or geotechnical issues.
 +
* '''Verifying Concerns:'''  Measure LNAPL transmissivity to determine if it is recoverable; measure vertical and horizontal separation distances between buildings and LNAPL bodies to screen for vapor intrusion concerns.
 +
* '''Remediation Goals:'''  Reduce mobile LNAPL saturation, abate unacceptable soil concentrations, terminate LNAPL body migration, abate unacceptable constituent concentrations in dissolved and vapor phases.  
 +
* '''Remediation Objectives:'''  Recover LNAPL to the extent practicable based on transmissivity, reduce soil concentrations to below regulatory limits, stop LNAPL migration with a barrier, contain migrating groundwater plume (if present), reduce groundwater and vapor concentration to acceptable levels.
 +
* '''Remediation Technologies:'''  LNAPL Mass Recovery technologies, LNAPL phase change technologies, LNAPL Mass Control technologies, combinations of technologies.
 +
 
 +
Overall, a LNAPL Conceptual Site Model that integrates key site specific information and current technical knowledge about LNAPL sites in general is instrumental to successful site management, where LNAPL concerns drive remediation goals, goals drive remediation objectives, and the objectives form the basis for the selection of remediation technologies.  
  
 
==References==
 
==References==
Line 123: Line 99:
  
 
==See Also==
 
==See Also==
 +

Revision as of 18:39, 21 August 2020

A Conceptual Site Model (CSM) is a collection of information about a contaminated site that integrates the available evidence regarding its hydrogeologic setting, contaminant sources, exposure pathways, potential receptors, and site history. A CSM for a Light Non-Aqueous Phase Liquid (LNAPL) site focuses on several key concepts: the stage in the LNAPL site life cycle, LNAPL distribution in the subsurface and the resulting mobility of the LNAPL, LNAPL as a source of dissolved and vapor plumes, and the attenuation of LNAPL sources over time.

Related Article(s)

CONTRIBUTOR(S): Charles Newell

Key Resource(s):

  • LNAPL Site Management: LCSM Evolution, Decision Process, and Remedial Technologies. LNAPL-3. ITRC.[1]
  • Managing Risk at LNAPL Sites - Frequently Asked Questions, 2nd Edition. API.[2]

Life Cycle of LNAPL Sites

Figure 1. Early, Middle, and Late Stage LNAPL releases[2]. The key distinctions are the presence of continuous LNAPL that can be mobile and the amount of time that has elapsed for NSZD to remove LNAPL.

A Conceptual Site Model (CSM) is a collection of information about a contaminated site that integrates the available evidence regarding its hydrogeologic setting, contaminant sources, exposure pathways, potential receptors, and site history (see ASTM E1689-95(2014)[3] and ASTM E2531-06(2014)[4]). When developing a CSM for an LNAPL site, it is important to understand that LNAPL releases evolve and change from what are referred to as Early Stage sites to Middle Stage and then to Late Stage sites[2] (Figure 1).

An Early Stage site is characterized by the presence of a continuous LNAPL zone where a thick layer of LNAPL accumulation (also known as free product) is observed in monitoring wells. The continuous LNAPL zone (or LNAPL body) may be mobile at Early Stage sites, migrating into previously non-impacted areas. Removal of significant LNAPL mass by active pumping may be feasible at these sites. Early Stage sites are now relatively rare in the United States due to stringent environmental regulations enacted in the 1980s which emphasized preventing releases.

Figure 2a. Time lapse conceptualization of the formation of an LNAPL body[5].
Figure 2b. Sand tank experiment of an LNAPL release[5].

Many sites in the U.S. are now considered to be in the Middle Stage, where the LNAPL thickness in wells has been largely depleted by natural spreading of the LNAPL body, Natural Source Zone Depletion (NSZD), smearing of the water table, and/or active remediation, and where the LNAPL bodies are stable or shrinking[1][2] (Figure 1). Active pumping characteristically only recovers LNAPL at relatively low rates of under 100 gallons per acre per year at Middle Stage sites, but NSZD rates may be much higher, on the order of 100s to 1,000s of gallons per acre per year. Middle Stage dissolved phase plumes, typically comprised of monoaromatics such as benzene, toluene, ethyl benzene, and xylenes, are stable or shrinking over time.

Late Stage sites only have a sparse distribution of residual (trapped) LNAPL due to long-term NSZD and any active remediation that has been performed at the site. The potential risks to receptors are typically low at Late Stage sites due to relatively low concentrations of LNAPL constituents in the dissolved phase and/or vapor plumes.

LNAPL Body Formation

LNAPLs released from tanks, pits, pipelines, or other sources will percolate downwards under the influence of gravity through permeable pathways in the unsaturated zone (e.g., soil pore space, fractures, and macropores) depending on the volume and pressure head of the LNAPL release, until encountering an impermeable layer or the water table, causing the LNAPL body to spread laterally. The Interstate Technology and Regulatory Council (ITRC)[1] describes this downward movement toward the water table this way:

During the downward movement of LNAPL through the soil, the presence of confining layers, subsurface heterogeneities, or other preferential pathways may result in irregular and complex lateral spreading and/or perching of LNAPL before the water table is encountered. Once at the water table, the LNAPL will spread laterally in a radial fashion as well as penetrate vertically downward into the saturated zone, displacing water to some depth proportional to the driving force of the vertical LNAPL column (or LNAPL head). The vertical penetration of LNAPL into the saturated zone will continue to occur as long as the downward force produced by the LNAPL head or pressure from the LNAPL release exceeds the counteracting forces produced by the resistance of the soil matrix and the buoyancy resulting from the density difference between LNAPL and groundwater.[1]

While the release at the surface is still active, the LNAPL body can expand until the LNAPL addition rate is equal to the NSZD depletion rate. However, once the release at the surface is stopped, the expansion will stop relatively quickly, and the LNAPL body will stabilize. Figure 2a shows a conceptual depiction of this release scenario and Figure 2b shows a sand tank experiment of an LNAPL release. Because of the buoyancy effects, LNAPL releases that reach the water table will form LNAPL bodies that “like icebergs, are partially above and below the water table”.[2]

Key Implications of the LNAPL Conceptual Site Model

The nature of multi-phase flow processes in porous media (e.g., the interaction of LNAPL, water, and air in the pore spaces of an unconsolidated aquifer) has several important implications for environmental professionals in areas including interpretation of LNAPL thickness in monitoring wells and assessment of the long-term risk associated with LNAPL source zones. A few of the key implications are described below.

Three States of LNAPL

LNAPL can be found in the subsurface in three different states:

  1. Residual LNAPL is trapped and immobile but can undergo composition and phase changes and generate dissolved hydrocarbon plumes in saturated zones and/or vapors in unsaturated zones. The fraction of the total pore space occupied by this discontinuous LNAPL is referred to as the residual saturation, with other phases such as water and air in the remainder of the pore space.
  2. Mobile LNAPL is LNAPL at greater than the residual saturation. Mobile LNAPL can accumulate in a well and is potentially recoverable, but is not migrating (i.e., the LNAPL body is not expanding).
  3. Migrating LNAPL is LNAPL at greater than the residual concentration which is observed to expand into previously non-impacted locations over time (e.g., LNAPL appears in a monitoring well that had previously been clean).

These three LNAPL states can cause different concerns and in some cases require different remediation goals.

LNAPL “Apparent Thickness” is a Poor Metric for Risk Management

Figure 3. Five LNAPL Thickness Scenarios for five different physical settings[2].
Figure 4. Apparent LNAPL thickness versus LNAPL transmissivity, showing no correlation[6].

LNAPL thickness in monitoring wells is often referred to as the “apparent LNAPL thickness” because at first glance this LNAPL thickness might be expected to be the thickness of LNAPL that is in the formation, but in reality it is not well correlated with the thickness of the LNAPL zone in the subsurface for several reasons.

First, different physical settings can produce different LNAPL thicknesses in monitoring wells. Sale et al. (2018) show five different scenarios that produce very different responses with regard to apparent LNAPL thickness (Figure 3). Scenario A shows an LNAPL apparent thickness in the monitoring well that is at static equilibrium with LNAPL in an unconfined aquifer. Scenario B, while also an unconfined aquifer, is comprised of very fine-grained soils that cause the LNAPL thickness in the well to be much higher than in Scenario A. In Scenario C, the LNAPL has accumulated under a confined unit (likely due to an underground release of LNAPL below the confining unit), and the LNAPL has risen above the groundwater potentiometric surface, leading to a large (and misleading) LNAPL thickness in the monitoring well. Scenario D, LNAPL in a perched unit, also shows a very different response from the other scenarios. Scenario E, LNAPL in fractured system, shows that the LNAPL can penetrate below the water table, and that LNAPL thickness in a well is dependent on the pressure from accumulation of LNAPL in the fractures[2].

Second, apparent LNAPL thickness is affected by changes in the groundwater surface elevation (or water table). Generally, when groundwater elevations are higher than typical, the LNAPL thickness in monitoring wells will decrease or go to zero because the groundwater will redistribute any mobile LNAPL into what previously was the unsaturated zone. During lower groundwater elevation periods, much more of the LNAPL will occur as a continuous phase near the water table, leading to higher LNAPL thicknesses in wells.

Overall, LNAPL thickness measurements are useful for delineating the extent of mobile LNAPL in the saturated zone and can provide useful data for understanding the vertical distribution of LNAPL in the formation[7][8]. But LNAPL thickness by itself is a very poor indicator of the feasibility of LNAPL recovery[9][6] (see NAPL Mobility) (Figure 4). Because there is little correlation between apparent LNAPL thickness and LNAPL mobility, there is also little correlation between apparent thickness and the risk to receptors from the LNAPL.

Complete LNAPL Remediation Is Very Challenging

Sale et al. (2018) described the problems with attaining complete LNAPL remediation this way:

Experience of the last few decades has taught us: 1) our best efforts often leave some LNAPL in place, and 2) the remaining LNAPL often sustains exceedances of drinking water standards in release areas for extended periods. Entrapment of LNAPLs at residual saturations is a primary factor constraining our success. Other challenges include the low solubility of LNAPL, the complexity of the subsurface geologic environment, access limitations associated with surface structures, and concentration goals that are often three to five orders of magnitude less than typical initial concentrations within LNAPL zones.[2]

In particular, the discontinuous residual LNAPL cannot be removed (or recovered) by pumping, and in situ remediation is expensive and not completely effective (see LNAPL Remediation Technologies). However, many regulatory programs require “LNAPL recovery to the extent practicable.” The lack of quantitative metrics and the lack of correlation between apparent LNAPL thicknesses and subsurface LNAPL makes this a problematic requirement in many cases and the ITRC (2018) cautions “Thickness or concentration data alone may not provide a sound basis for defining the point at which a cleanup objective is achieved.”[1] However, Sale et al. (2018) describe metrics such as LNAPL transmissivity, limited/infrequent well thicknesses, decline curve analysis, asymptotic analysis, and comparison to NSZD rates that can be used to determine when LNAPL has been removed the extent practicable[2].

Attenuation Processes are Active and Important

Both LNAPL source zones and their dissolved phase hydrocarbon plumes are attenuated by biodegradation and other attenuation process. In the source zone, this attenuation is called Natural Source Zone Depletion (NSZD) (see also Natural Attenuation in Source Zone and Groundwater Plume - Bemidji Crude Oil Spill). In the dissolved plume it is called Monitored Natural Attenuation (MNA) (see also Biodegradation - Hydrocarbons). These processes generally limit the length of dissolved phase hydrocarbon plumes to a few hundred feet[10] via processes that have been well known and understood since the mid-1990s.

However, NSZD is “by far, the biggest new idea for LNAPLs in the last decade.”[2] Originally, LNAPL bodies were thought to attenuate very slowly via dissolution and volatilization. In 2006, it was discovered that NSZD rates are orders of magnitude higher than originally thought, largely due to direct biodegradation of LNAPL constituents to methane and carbon dioxide by methanogenic consortiums of naturally occurring bacteria[11][12]. NSZD processes play an important role in risk mitigation and the long-term stability of LNAPL bodies[13][1].

Risk from LNAPL Source Zones Diminishes Over Time

At Early Stage LNAPL sites, the expansion of the LNAPL body is a risk that needs to be addressed. Fortunately, this type of site is relatively rare. For Middle and Late Stage sites, the primary risks are associated with phase changes (dissolution of the LNAPL forming a dissolved plume and volatilization from the LNAPL or dissolved plume forming hydrocarbon vapors). As described above, MNA can often control the dissolved phase (see Monitored Natural Attenuation (MNA) of Fuels), while aerobic biodegradation in the unsaturated zone greatly reduces the vapor intrusion risk from hydrocarbon vapors (see Vapor Intrusion - Separation Distances from Petroleum Sources).

Understanding LNAPL body mobility and stability is important to understand the potential risks posed by LNAPL. The relative magnitude of LNAPL mobility can be determined by measuring the LNAPL transmissivity (see NAPL Mobility). If the transmissivity is below a threshold level (in the range of 0.1 to 0.8 ft2/day) then the LNAPL likely cannot be recovered efficiently by pumping, but above this transmissivity level recovery is feasible[1]. Michigan’s LNAPL guidance states “if the NAPL has a transmissivity greater than 0.5 ft2/day, it is likely that the NAPL can be recovered in a cost-effective and efficient manner unless a demonstration is made to show otherwise.” Kansas LNAPL guidance requires “recovery of all LNAPL with a transmissivity greater than 0.8 ft2/day that can be recovered in an efficient, cost-effective manner.”[1]. The stability of the entire LNAPL body can be evaluated using statistical tools to determine if migration of LNAPL is occurring[14].

Overview of Modern LNAPL Conceptual Site Model

Figure 5. A higher tier of LNAPL CSM is useful as LNAPL site complexity increases[1].

The ITRC (2018) describes the typical evolution of an LCSM over the course of the remediation process which can be broken into three separate stages:

  • An Initial LCSM focuses on identifying the LNAPL concerns, such as a risk to health or safety, any LNAPL migration, LNAPL-specific regulations, and physical or aesthetic impacts.
  • A Remedy Selection LCSM supports remedial technology evaluation by characterizing aspects of the LNAPL and site subsurface that may impact remedial technology performance.
  • A Design and Performance LCSM focuses on presenting the technical information needed to establish remediation objectives, design and implement remedies or control measures, and track progress toward defined remediation endpoints.

One key question when developing an LCSM is “how much data is enough.” In general, the answer is that the existing data is sufficient for the current stage of the remediation project when it allows the stakeholders to agree on a path forward[1]. Figure 5 shows that as the level of complexity of a site increases, a higher tier of LCSM is useful to provide enough information for making decisions[1][3]. The higher tier of information could be higher data density, additional tools for a given line of evidence, or other evaluations.

LNAPL Concerns, Remediation Goals and Objectives

Finally, the ITRC (2018) provides a methodology for identifying LNAPL concerns, verifying those concerns, selecting LNAPL remediation goals, and determining LNAPL remediation objectives. Examples of each of these concepts are provided below:

  • Potential Concerns: Human or ecological risk concerns, fire or explosivity issues, LNAPL migration, LNAPL-specific regulatory concerns, other concerns such as odors or geotechnical issues.
  • Verifying Concerns: Measure LNAPL transmissivity to determine if it is recoverable; measure vertical and horizontal separation distances between buildings and LNAPL bodies to screen for vapor intrusion concerns.
  • Remediation Goals: Reduce mobile LNAPL saturation, abate unacceptable soil concentrations, terminate LNAPL body migration, abate unacceptable constituent concentrations in dissolved and vapor phases.
  • Remediation Objectives: Recover LNAPL to the extent practicable based on transmissivity, reduce soil concentrations to below regulatory limits, stop LNAPL migration with a barrier, contain migrating groundwater plume (if present), reduce groundwater and vapor concentration to acceptable levels.
  • Remediation Technologies: LNAPL Mass Recovery technologies, LNAPL phase change technologies, LNAPL Mass Control technologies, combinations of technologies.

Overall, a LNAPL Conceptual Site Model that integrates key site specific information and current technical knowledge about LNAPL sites in general is instrumental to successful site management, where LNAPL concerns drive remediation goals, goals drive remediation objectives, and the objectives form the basis for the selection of remediation technologies.

References

  1. ^ 1.00 1.01 1.02 1.03 1.04 1.05 1.06 1.07 1.08 1.09 1.10 Interstate Technology and Regulatory Council (ITRC), 2018. LNAPL Site Management: LCSM Evolution, Decision Process, and Remedial Technologies. LNAPL-3. ITRC, LNAPL Update Team, Washington, DC. LNAPL-3 Website
  2. ^ 2.0 2.1 2.2 2.3 2.4 2.5 2.6 2.7 2.8 2.9 Sale, T., Hopkins, H., and Kirkman, A., 2018. Managing Risk at LNAPL Sites - Frequently Asked Questions, 2nd Edition. American Petroleum Institute (API), Washington, DC. 72 pages. Free download from API. Report.pdf
  3. ^ 3.0 3.1 ASTM, 2014. Standard Guide for Developing Conceptual Site Models for Contaminated Sites. ASTM E1689-95(2014), ASTM International, West Conshohocken, PA. DOI: 10.1520/E1689-95R14 http://www.astm.org/cgi-bin/resolver.cgi?E1689
  4. ^ ASTM, 2014. Standard Guide for Development of Conceptual Site Models and Remediation Strategies for Light Nonaqueous-Phase Liquids Released to the Subsurface. ASTM E2531-06(2014), ASTM International, West Conshohocken, PA. DOI: 10.1520/E2531-06R14 http://www.astm.org/cgi-bin/resolver.cgi?E2531
  5. ^ 5.0 5.1 Interstate Technology and Regulatory Council (ITRC), 2019. LNAPL Training: Connecting the Science to Managing Sites. Part 1: Understanding LNAPL Behavior in the Subsurface. ITRC, Washington, DC. Slides.pdf
  6. ^ 6.0 6.1 Hawthorne, J.M., 2015. Nationwide (USA) Statistical Analysis of LNAPL Transmissivity, in: R. Darlington and A.C. Barton (Chairs), Bioremediation and Sustainable Environmental Technologies—2015. Third International Symposium on Bioremediation and Sustainable Environmental Technologies (Miami, FL), page C-017, Battelle Memorial Institute, Columbus, OH. www.battelle.org/biosymp Abstract.pdf
  7. ^ Hawthorne, J.M., 2011. Diagnostic Gauge Plots—Simple Yet Powerful LCSM Tools. Applied NAPL Science Review (ANSR), 1(2). Website Report.pdf
  8. ^ Kirkman, A.J., Adamski, M., and Hawthorne, M., 2013. Identification and Assessment of Confined and Perched LNAPL Conditions. Groundwater Monitoring and Remediation, 33 (1), pp. 75–86. DOI:10.1111/j.1745-6592.2012.01412.x
  9. ^ Interstate Technology and Regulatory Council (ITRC), 2009. Evaluating LNAPL Remedial Technologies for Achieving Project Goals. LNAPL-2. ITRC, LNAPLs Team, Washington, DC. www.itrcweb.org Report.pdf
  10. ^ Newell, C.J., and Connor, J.A., 1998. Characteristics of Dissolved Hydrocarbon Plumes: Results from Four Studies, Version 1.1. American Petroleum Institute, Soil/Groundwater Technical Task Force, Washington, DC. Report.pdf
  11. ^ Lundegard, P.D., and Johnson, P.C., 2006. Source Zone Natural Attenuation at Petroleum Spill Sites—II: Application to a Former Oil Field. Groundwater Monitoring and Remediation. 26(4), pp. 93-106. [ https://doi.org/10.1111/j.1745-6592.2006.00115.x DOI: 10.1111/j.1745-6592.2006.00115.x]
  12. ^ Garg, S., Newell, C., Kulkarni, P., King, D., Adamson, D.T., Irianni Renno, M., and Sale, T., 2017. Overview of Natural Source Zone Depletion: Processes, Controlling Factors, and Composition Change. Groundwater Monitoring and Remediation, 37(3), pp. 62-81. DOI: 10.1111/gwmr.12219 Report.pdf
  13. ^ Mahler, N., Sale, T., and Lyverse, M., 2012. A Mass Balance Approach to Resolving LNAPL Stability. Groundwater, 50(6), pp 861-871. DOI: 10.1111/j.1745-6584.2012.00949.x
  14. ^ Hawthorne, J.M., Stone, C.D., Helsel, D., 2013. LNAPL Body Stability Part 2: Daughter Plume Stability via Spatial Moments Analysis. Applied NAPL Science Review (ANSR), 3(5). Website Report.pdf

See Also