Zerovalent Iron Permeable Reactive Barriers - Revision history

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Jhurley: /* Zerovalent Iron */

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‎Zerovalent Iron

Jhurley at 21:22, 28 January 2019

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Debra Tabron at 20:19, 23 January 2019

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Debra Tabron: Created page with "Permeable reactive barriers (PRBs) are ''in situ'' treatment zones created below ground to clean up contaminated groundwater. PRBs take advantage of natural groundwater migrat..."

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Permeable reactive barriers (PRBs) are ''in situ'' treatment zones created below ground to clean up contaminated groundwater. PRBs take advantage of natural groundwater migration to transport contaminants to a defined treatment zone. Contaminants are removed from groundwater in the PRB and treated groundwater passes through the permeable zone; eventually a “clean front” is created on the down-gradient side of the PRB. Zerovalent Iron (ZVI) was the first reactive material used in PRBs for groundwater remediation and it continues to be the primary material used in the construction of these treatment systems. ZVI PRBs can treat groundwater contaminated with chlorinated solvents and their breakdown products such as tetrachloroethene (PCE), trichloroethene (TCE), ''cis''-1,2-dichloroethene (''cis''-DCE), vinyl chloride (VC), 1,1,1-trichloroethane (1,1,1-TCA), 1,1-dichloroethane (1,1-DCA), 1,2-dichloroethane (1,2-DCA), chloroform, and carbon tetrachloride; explosives such as TNT and RDX; cations of Pb, Cd, Ni, Zn, and Hg; and anions of Cr, As, Sb, Se, U, and Tc.

<div style="float:right;margin:0 0 2em 2em;">__TOC__</div>

'''Related Article(s):'''
*[[Zerovalent Iron (ZVI) (Chemical Reduction - ISCR)]]
*[[Chemical Reduction (In Situ - ISCR)]]
*[[Metal and Metalloids - Remediation]]
*[[Chlorinated Solvents]]

'''CONTRIBUTOR(S):'''

'''Key Resource(s)''':
*[[media:2005-ITRC_Permeable_Reactive_Barriers.pdf| Permeable Reactive Barriers: Lessons Learned/New Directions. Interstate Technology Regulatory Council (2005)]]<ref name= "ITRC2005W">Interstate Technology & Regulatory Council (ITRC), 2005. Permeable Reactive Barriers: Lessons Learned/New Directions. PRB-4. Washington, D.C.: Interstate Technology & Regulatory Council, Permeable Reactive Barriers Team.[[media:2005-ITRC_Permeable_Reactive_Barriers.pdf| Report.pdf]]</ref>.
*[[media:ITRC-2011-PRB_Tech_Update.pdf| Permeable Reactive Barrier: Technology Update. Interstate Technology Regulatory Council (2011)]]<ref name= "ITRC2011W">Interstate Technology & Regulatory Council (ITRC), 2011. Permeable Reactive Barrier: Technology Update. PRB-5. Washington, D.C.: Interstate Technology & Regulatory Council, PRB: Technology Update Team. [[media:ITRC-2011-PRB_Tech_Update.pdf| Report.pdf]]</ref>

==Introduction==
A PRB is commonly constructed using granular iron, limestone, organic-carbon, zeolites, apatite, or mixtures of these materials with sand or gravel<ref name= "ITRC2005W"/><ref name= "ITRC2011W"/>. PRBs are installed hydraulically down-gradient from contaminant source zones to prevent off-site plume migration or to protect sensitive receptors. Design considerations for PRBs include:
#understanding contaminant flux to determine the residence time requirement for effective treatment;
#understanding geochemical conditions to identify compatibility issues between the selected reactive medium and site-specific groundwater; and
#understanding groundwater flow to ensure the contaminant plume is intercepted for treatment (See Fig. 1) so contaminant flow beneath, around, or above the treatment system does not occur. PRBs are generally keyed into impermeable hydrostratigraphic units, such as clay layers or bedrock, to prevent underflow of contaminants beneath the treatment zone.

[[File:Wilkin1w2 Fig1.png|thumb|Figure 1. Conceptual Model of PRB. Adapted from Wilkin, et al., 2002<ref>Wilkin, R T., Puls, R W. P and Sewell, G W. Environmental Research Brief: Long-term Performance of Permeable Reactive Barriers Using Zero-valent Iron: An Evaluation at Two Sites. US EPAU.S. Environmental Protection Agency, Washington, DC, EPA/600/S-02/001, 2002. [[media:2002-Wilkin-Long-term_Perf_of_Permeable_Reactive_Barriers_Using_Zero-valent.pdf| Report.pdf]]</ref>]]

==Zerovalent Iron==
The first field-scale test of a PRB constructed with ZVI was conducted in 1991 at the Canadian Forces Base, Borden, Ontario by researchers from the University of Waterloo<ref>Gillham, R.W. and O'Hannesin, S.F., 1994. Enhanced degradation of halogenated aliphatics by zero‐valent iron. Groundwater, 32(6), pp.958-967. [https://doi.org/10.1111/j.1745-6584.1994.tb00935.x doi: 10.1111/j.1745-6584.1994.tb00935.x]</ref><ref>O'Hannesin, S.F. and Gillham, R.W., 1998. Long‐term performance of an in situ “iron wall” for remediation of VOCs. Groundwater, 36(1), pp.164-170. [https://doi.org/10.1111/j.1745-6584.1998.tb01077.x doi: 10.1111/j.1745-6584.1998.tb01077.x]</ref>. The first full-scale ZVI-based PRB was constructed in Sunnyvale, California in 1994 to treat groundwater contaminated with TCE and ''cis''-DCE<ref name= "Warner2005">Warner, S.D., Longino, B.L., Zhang, M.I.A.O., Bennett, P., Szerdy, F.S. and Hamilton, L.A., 2005. The first commercial permeable reactive barrier composed of granular iron: hydraulic and chemical performance at 10 years of operation. IAHS Publication, 298, p.32 - 42. ISBN 1-901502-23-6]</ref>. Long-term performance studies have documented sustained removal of trichloroethene and hexavalent chromium by ZVI PRBs and their continued hydraulic performance for up to 15 years<ref name= "Warner2005"/><ref>Phillips, D.H., Nooten, T.V., Bastiaens, L., Russell, M.I., Dickson, K., Plant, S., Ahad, J.M.E., Newton, T., Elliot, T. and Kalin, R.M., 2010. Ten year performance evaluation of a field-scale zero-valent iron permeable reactive barrier installed to remediate trichloroethene contaminated groundwater. Environmental Science & Technology, 44(10), pp.3861-3869. [https://doi.org/10.1021/es902737t doi: 10.1021/es902737t]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Puls, R.W., Lee, T.R. and Woods, L.L., 2014. Fifteen-year assessment of a permeable reactive barrier for treatment of chromate and trichloroethylene in groundwater. Science of the Total Environment, 468, pp.186-194. [https://doi.org/10.1016/j.scitotenv.2013.08.056 doi: 10.1016/j.scitotenv.2013.08.056]</ref>.

ZVI degrades chlorinated ethenes, ethanes, and methanes via reductive abiotic reactions that largely circumvent the production of toxic chlorinated daughter compounds, such as vinyl chloride, which can be produced during biological reduction<ref>Matheson, L.J. and Tratnyek, P.G., 1994. Reductive dehalogenation of chlorinated methanes by iron metal. Environmental Science & Technology, 28(12), pp.2045-2053. [http://dx.doi.org/10.1021/es00061a012 doi:10.1021/es00061a012]</ref><ref name= "Arnold2000">Arnold, W.A. and Roberts, A.L., 2000. Pathways and kinetics of chlorinated ethylene and chlorinated acetylene reaction with Fe (0) particles. Environmental Science & Technology, 34(9), pp.1794-1805. [https://doi.org/10.1021/es990884q doi: 10.1021/es990884q]</ref>. For example, Arnold and Roberts<ref name= "Arnold2000"/> reported that >85% of PCE and >90% of TCE treatment by zerovalent iron is accounted for by β-elimination reactions that avoid production of ''cis''-DCE and VC.

Zerovalent Iron has also been used in pilot or full-scale tests to treat groundwater contaminated with metals (e.g., chromium), metalloids (e.g., arsenic), and radionuclides (e.g., uranium)<ref>Blowes, D.W., Ptacek, C.J., Benner, S.G., McRae, C.W., Bennett, T.A. and Puls, R.W., 2000. Treatment of inorganic contaminants using permeable reactive barriers. Journal of Contaminant Hydrology, 45(1), pp.123-137</ref><ref>Puls, R.W., Paul, C.J. and Powell, R.M., 1999. The application of in situ permeable reactive (zero-valent iron) barrier technology for the remediation of chromate-contaminated groundwater: a field test. Applied Geochemistry, 14(8), pp.989-1000. [https://doi.org/10.1016/S0883-2927(99)00010-4 doi: 10.1016/s0883-2927(99)00010-4]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Beak, D.G. and Lee, T.R., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 1. Hydrogeochemical studies. Journal of Contaminant Hydrology, 106(1-2), pp.1-14. [https://doi.org/10.1016/j.jconhyd.2008.12.002 doi: 10.1016/j.jconhyd.2008.12.002]</ref><ref>Morrison, S.J., Metzler, D.R. and Carpenter, C.E., 2001. Uranium precipitation in a permeable reactive barrier by progressive irreversible dissolution of zerovalent iron. Environmental Science & Technology, 35(2), pp.385-390. [https://doi.org/10.1021/es001204i doi: 10.1021/es001204i]</ref>. Contaminant removal processes are complex and involve a combination of sorption to the surface of the ZVI or secondary minerals formed in the PRB, reductive precipitation, and co-precipitation. Other possible uses of ZVI for groundwater include treatment of explosives such as nitro aromatic compounds<ref>Agrawal, A. and Tratnyek, P.G., 1995. Reduction of nitro aromatic compounds by zero-valent iron metal. Environmental Science & Technology,30(1), pp.153-160. [http://dx.doi.org/10.1021/es950211h doi:10.1021/es950211h]</ref><ref>Scherer, M.M., Johnson, K.M., Westall, J.C. and Tratnyek, P.G., 2001. Mass transport effects on the kinetics of nitrobenzene reduction by iron metal. Environmental Science & Technology, 35(13), pp.2804-2811. [https://doi.org/10.1021/es0016856 doi: 10.1021/es0016856]</ref>. Treatment applications of ZVI for organic and inorganic contaminants encountered in groundwater at hazardous waste sites are summarized in Table 1.

{| class="wikitable" style="text-align: left;"
{| class="wikitable" style="margin-left: auto; margin-right: auto; border: none;
|+ <div style="text-align: center;"> Table 1. Groundwater Contaminants Treated by Granular ZVI</div>
|-
! Contaminant Class
! Contaminant
! Removal Mechanism
|-
| Chlorinated Ethenes || Tetrachloroethene, PCE Trichloroethene, TCE ''cis''-1,2-Dichloroethene, ''cis''-DCE ''trans''-1,2-Dichloroethene, ''trans''-DCE 1,1- Dichloroethene, 1,1-DCE Vinyl Chloride, VC || α-elimination β-elimination Hydrogenolysis
|-
| Chlorinated Ethanes || Hexachloroethane, HCA 1,1,1,2-Tetrachloroethane, 1,1,1,2-TeCA 1,1,2,2-Tetrachloroethane, 1,1,2,2-TeCA 1,1,1-Trichloroethane, 1,1,1-TCA 1,1-Dichloroethane, 1,1-DCA || α-elimination β-elimination Hydrogenolysis
|-
| Chlorinated Methanes || Tetrachloromethane, CT Trichloromethane, TCM || α-elimination β-elimination Hydrogenolysis
|-
| Explosives || Trinitrotoluene (TNT) Hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX) || Adsorption Reduction to 2,4,6-triaminotoluene (TAT)
|-
| Anionic Metals || Chromium Arsenic Antimony Selenium Uranium Technetium || Reductive precipitation Co-precipitation Adsorption
|-
| Metals || Lead Cadmium Nickel Zinc Mercury || Precipitation Co-precipitation Adsorption
|}

==PRB Design and Site Conditions==
Like other ''in-situ'' technologies used for groundwater cleanup, PRB designs rely on accurate site characterization data for geology, hydrology, and groundwater geochemistry. Site hydrologic aspects critical for PRB design and performance include seasonal consistency in groundwater flow direction to maintain migration of contaminants to the PRB at an appropriate flow velocity. High flow velocities (≳2 m/d) can result in short residence time in the treatment zone and early breakthrough of contaminants; low flow velocities (≲0.1 m/d) result in little change in contaminant concentrations over time, so wells in down-gradient regions respond slowly.
Geochemical considerations for the design of ZVI PRBs include redox conditions and the concentrations and make up of major ions dissolved in local groundwater. Geochemical conditions that are favorable for the sustained performance of ZVI PRBs include:

Dissolved O2 concentrations ≲2 mg/L: Excess dissolved oxygen leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure.

Nitrate-N concentrations ≲10 mg/L: Like dissolved oxygen, nitrate enhanced iron corrosion leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure<ref>Liang, L., Moline, G.R., Kamolpornwijit, W. and West, O.R., 2005. Influence of hydrogeochemical processes on zero-valent iron reactive barrier performance: A field investigation. Journal of Contaminant Hydrology, 78(4), pp.291-312. [https://doi.org/10.1016/j.jconhyd.2005.05.006 doi: 10.1016/j.jconhyd.2005.05.006]</ref>.

Bicarbonate alkalinity ≲250 mg CaCO3/L: Carbonate minerals (aragonite, siderite, chukanovite, carbonate-green rust) precipitate in the moderately alkaline pH environment (pH~10) produced by ZVI PRBs and most of the porosity and reactivity reduction in PRBs can be accounted for by these minerals (see Figure 2)<ref>Jeen, S.W., Gillham, R.W. and Blowes, D.W., 2006. Effects of carbonate precipitates on long-term performance of granular iron for reductive dechlorination of TCE. Environmental Science & Technology, 40(20), pp.6432-6437. [https://doi.org/10.1021/es0608747 doi: 10.1021/es0608747]</ref><ref>Li, L., Benson, C.H. and Lawson, E.M., 2006. Modeling porosity reductions caused by mineral fouling in continuous-wall permeable reactive barriers. Journal of Contaminant Hydrology, 83(1-2), pp.89-121. [https://doi.org/10.1016/j.jconhyd.2005.11.004 doi: 10.1016/j.jconhyd.2005.11.004]</ref><ref>Parbs, A., Ebert, M. and Dahmke, A., 2007. Long-term effects of dissolved carbonate species on the degradation of trichloroethylene by zerovalent iron. Environmental Science & Technology, 41(1), pp.291-296. [https://doi.org/10.1021/es061397v doi: 10.1021/es061397v]</ref><ref>Henderson, A.D. and Demond, A.H., 2007. Long-term performance of zero-valent iron permeable reactive barriers: a critical review. Environmental Engineering Science, 24(4), pp.401-423. [https://doi.org/10.1089/ees.2006.0071 doi: 10.1089/ees.2006.0071]</ref>.

Sulfate concentrations ≳100 mg/L: High dissolved hydrogen generated by iron corrosion creates a favorable environment for sulfate-reducing bacteria and methane-producing archaea. Metal sulfide precipitates like mackinawite (FeS) provide a source of secondary reactivity for chlorinated solvents and metals<ref>Butler, E.C. and Hayes, K.F., 1999. Kinetics of the transformation of trichloroethylene and tetrachloroethylene by iron sulfide. Environmental Science & Technology, 33(12), pp.2021-2027. [http://dx.doi.org/10.1021/es9809455 doi: 10.1021/es9809455]</ref><ref>Beak, D.G. and Wilkin, R.T., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 2. Geochemical modeling and solid phase studies. Journal of Contaminant Hydrology, 106(1-2), pp.15-28. [https://doi.org/10.1016/j.jconhyd.2008.12.003 doi: 10.1016/j.jconhyd.2008.12.003]</ref>. Thus, levels of sulfate in influent groundwater promote natural sulfidation of ZVI PRBs and potentially enhanced treatment capacity<ref>Fan, D., Lan, Y., Tratnyek, P.G., Johnson, R.L., Filip, J., O’Carroll, D.M., Nunez Garcia, A. and Agrawal, A., 2017. Sulfidation of iron-based materials: A review of processes and implications for water treatment and remediation. Environmental Science & Technology, 51(22), pp.13070-13085. [https://doi.org/10.1021/acs.est.7b04177 doi: 10.1021/acs.est.7b04177]</ref>.

Total dissolved solids below ≲1500 mg/L: The amount of secondary mineralization and clogging potential increases with increasing solute levels.

[[File:Wilkin1w2 Fig2.png|thumb|Figure 2. False-color scanning electron micrograph<ref>ESTCP, 2018. Analysis of Long-Term Performance of Zero-valent Iron Applications. Project Report #ER-201589-PR. [[media:2018-ESTCP_Analysis_of_Long-Term_performance_of_Zero-valent_Iron_App.pdf| Report.pdf]]</ref> of a zero-valent iron grain (pink) coated with secondary precipitates (iron oxide and aragonite; green) surrounded by native aquifer quartz grains (blue). The iron particle is approximately 1.5 mm in length. ]]

==Performance Monitoring==
Performance monitoring of PRBs typically includes: 1) sampling groundwater monitoring wells located up-gradient of the PRB to establish influent contaminant concentrations and groundwater geochemistry; 2) sampling groundwater monitoring wells located within the PRB to establish in-wall behavior; and, 3) sampling groundwater monitoring wells located down-gradient of the PRB to establish contaminant concentrations and groundwater geochemistry in the effluent. Key monitoring parameters include: contaminant(s) and daughter product(s), pH, oxidation-reduction potential, specific conductance, alkalinity, calcium, iron, and sulfate. These monitoring parameters provide an indication of whether or not the expected geochemical environment is present within the treatment zone, and also that contaminant degradation is occurring.

For chlorinated solvents, analysis of the parent compounds and daughter products (e.g., ethene and ethane) aids in the performance analysis. Compound-specific isotope analysis can be helpful to understand contaminant degradation processes in complicated systems<ref>VanStone, N., Przepiora, A., Vogan, J., Lacrampe-Couloume, G., Powers, B., Perez, E., Mabury, S. and Lollar, B.S., 2005. Monitoring trichloroethene remediation at an iron permeable reactive barrier using stable carbon isotopic analysis. Journal of Contaminant Hydrology, 78(4), pp.313-325. [https://doi.org/10.1016/j.jconhyd.2005.05.013 doi: 10.1016/j.jconhyd.2005.05.013]</ref><ref>Lojkasek‐Lima, P., Aravena, R., Shouakar‐Stash, O., Frape, S.K., Marchesi, M., Fiorenza, S. and Vogan, J., 2012. Evaluating TCE abiotic and biotic degradation pathways in a permeable reactive barrier using compound specific isotope analysis. Groundwater Monitoring & Remediation, 32(4), pp.53-62. [https://doi.org/10.1111/j.1745-6592.2012.01403.x doi: 10.1111/j.1745-6592.2012.01403.x]</ref>.
Hydrologic monitoring typically consists of gradient analysis to determine flow directions and whether water level changes are abrupt in the vicinity of the PRB, indicating the potential for impeded groundwater flow. Core collection with solid-phase analysis and/or geophysical surveys (e.g., conductivity probing) are not common or routine components of performance monitoring, but can be considered in situations where anomalous behavior is encountered such as a failure to meet performance criteria.

Problems noted with the application of this, and other, ''in situ''technologies include:
*contaminants are present down-gradient of the PRB prior to installation;
*influent contaminant concentrations may increase with time such that necessary residence time requirements are not met;
*incomplete capture of the plume, especially along peripheries of the plume;
*unaccounted for high contaminant flux zones and early breakthrough; and,
*incomplete coverage of the reactive medium in the subsurface.
Many of these issues can be addressed with rigorous site characterization, which may incur extra cost and time prior to remediation, but can potentially avoid implementation of secondary measures.

==Summary & Outlook==
ZVI is perhaps the most widely studied and best understood reactive material used for groundwater remediation. It will continue to serve as a benchmark for other novel treatment media and for studying treatment options for emerging contaminants. The environmental industry is becoming accustomed to screening sites for potential ZVI applications and is actively taking advantage of improving ZVI performance, i.e., through natural sulfidation and treating up-gradient sources of contamination to extend the lifetime of the PRB. Advantages of using ZVI in PRBs for remediating contaminated groundwater include: wide range of treatable contaminants (organics and inorganics); expectation of complete subsurface coverage; and, flexible adaptation to variable contaminant flux and plume geometry. Disadvantages include: construction challenges and uncertainty in predicting long-term treatment and hydraulic performance. These uncertainties can often be addressed with rigorous site characterization.

==References==
<references />

← Older revision		Revision as of 02:05, 28 April 2022
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−	'''~~CONTRIBUTOR~~(S):''' [[Dr. Richard Wilkin]]	+	'''Contributor(s):''' [[Dr. Richard Wilkin]]

@@ Line 23: / Line 23: @@
 #understanding groundwater flow to ensure the contaminant plume is intercepted for treatment (See Figure 1) so contaminant flow beneath, around, or above the treatment system does not occur. PRBs are generally keyed into impermeable hydrostratigraphic units, such as clay layers or bedrock, to prevent underflow of contaminants beneath the treatment zone.
-[[File:Wilkin1w2 Fig1.png|thumb|300px|Figure 1. Conceptual Model of PRB. Adapted from Wilkin, et al., 2002<ref>Wilkin, R T., Puls, R W. P and Sewell, G W.  Environmental Research Brief: Long-term Performance of Permeable Reactive Barriers Using Zero-valent Iron: An Evaluation at Two Sites. US EPAU.S. Environmental Protection Agency, Washington, DC, EPA/600/S-02/001, 2002. [[media:2002-Wilkin-Long-term_Perf_of_Permeable_Reactive_Barriers_Using_Zero-valent.pdf| Report.pdf]]</ref>]]
+[[File:Wilkin1w2 Fig1.png|thumb|400px|Figure 1. Conceptual Model of PRB. Adapted from Wilkin, et al., 2002<ref>Wilkin, R T., Puls, R W. P and Sewell, G W.  Environmental Research Brief: Long-term Performance of Permeable Reactive Barriers Using Zero-valent Iron: An Evaluation at Two Sites. US EPAU.S. Environmental Protection Agency, Washington, DC, EPA/600/S-02/001, 2002. [[media:2002-Wilkin-Long-term_Perf_of_Permeable_Reactive_Barriers_Using_Zero-valent.pdf| Report.pdf]]</ref>]]
 ==Zerovalent Iron==
@@ Line 30: / Line 30: @@
 ZVI degrades chlorinated ethenes, ethanes, and methanes via reductive abiotic reactions that largely circumvent the production of toxic chlorinated daughter compounds, such as vinyl chloride, which can be produced during biological reduction<ref>Matheson, L.J. and Tratnyek, P.G., 1994. Reductive dehalogenation of chlorinated methanes by iron metal. Environmental Science & Technology, 28(12), pp.2045-2053. [http://dx.doi.org/10.1021/es00061a012 doi:10.1021/es00061a012]</ref><ref name= "Arnold2000">Arnold, W.A. and Roberts, A.L., 2000. Pathways and kinetics of chlorinated ethylene and chlorinated acetylene reaction with Fe (0) particles. Environmental Science & Technology, 34(9), pp.1794-1805. [https://doi.org/10.1021/es990884q doi: 10.1021/es990884q]</ref>.  For example, Arnold and Roberts<ref name= "Arnold2000"/> reported that >85% of PCE and >90% of TCE treatment by zerovalent iron is accounted for by [[Wikipedia: Elimination reaction | &beta;-elimination reactions]] that avoid production of ''cis''-DCE and VC.
-{| class="wikitable" style="float: left; text-align: left; margin-right: 20px;"
+{| class="wikitable" style="float: left; text-align: left; margin-right: 30px;"
 |+ Table 1.  Groundwater Contaminants Treated by Granular ZVI
 |-

@@ Line 21: / Line 21: @@
 #understanding contaminant flux to determine the residence time requirement for effective treatment;
 #understanding geochemical conditions to identify compatibility issues between the selected reactive medium and site-specific groundwater; and
-#understanding groundwater flow to ensure the contaminant plume is intercepted for treatment (See Fig. 1) so contaminant flow beneath, around, or above the treatment system does not occur. PRBs are generally keyed into impermeable hydrostratigraphic units, such as clay layers or bedrock, to prevent underflow of contaminants beneath the treatment zone.
+#understanding groundwater flow to ensure the contaminant plume is intercepted for treatment (See Figure 1) so contaminant flow beneath, around, or above the treatment system does not occur. PRBs are generally keyed into impermeable hydrostratigraphic units, such as clay layers or bedrock, to prevent underflow of contaminants beneath the treatment zone.
-[[File:Wilkin1w2 Fig1.png|thumb|Figure 1. Conceptual Model of PRB. Adapted from Wilkin, et al., 2002<ref>Wilkin, R T., Puls, R W. P and Sewell, G W.  Environmental Research Brief: Long-term Performance of Permeable Reactive Barriers Using Zero-valent Iron: An Evaluation at Two Sites. US EPAU.S. Environmental Protection Agency, Washington, DC, EPA/600/S-02/001, 2002. [[media:2002-Wilkin-Long-term_Perf_of_Permeable_Reactive_Barriers_Using_Zero-valent.pdf| Report.pdf]]</ref>]]
+[[File:Wilkin1w2 Fig1.png|thumb|300px|Figure 1. Conceptual Model of PRB. Adapted from Wilkin, et al., 2002<ref>Wilkin, R T., Puls, R W. P and Sewell, G W.  Environmental Research Brief: Long-term Performance of Permeable Reactive Barriers Using Zero-valent Iron: An Evaluation at Two Sites. US EPAU.S. Environmental Protection Agency, Washington, DC, EPA/600/S-02/001, 2002. [[media:2002-Wilkin-Long-term_Perf_of_Permeable_Reactive_Barriers_Using_Zero-valent.pdf| Report.pdf]]</ref>]]
 ==Zerovalent Iron==
 The first field-scale test of a PRB constructed with ZVI was conducted in 1991 at the Canadian Forces Base, Borden, Ontario by researchers from the University of Waterloo<ref>Gillham, R.W. and O'Hannesin, S.F., 1994. Enhanced degradation of halogenated aliphatics by zero‐valent iron. Groundwater, 32(6), pp.958-967. [https://doi.org/10.1111/j.1745-6584.1994.tb00935.x doi: 10.1111/j.1745-6584.1994.tb00935.x]</ref><ref>O'Hannesin, S.F. and Gillham, R.W., 1998. Long‐term performance of an in situ “iron wall” for remediation of VOCs. Groundwater, 36(1), pp.164-170. [https://doi.org/10.1111/j.1745-6584.1998.tb01077.x doi: 10.1111/j.1745-6584.1998.tb01077.x]</ref>.  The first full-scale ZVI-based PRB was constructed in Sunnyvale, California in 1994 to treat groundwater contaminated with TCE and ''cis''-DCE<ref name= "Warner2005">Warner, S.D., Longino, B.L., Zhang, M.I.A.O., Bennett, P., Szerdy, F.S. and Hamilton, L.A., 2005. The first commercial permeable reactive barrier composed of granular iron: hydraulic and chemical performance at 10 years of operation. IAHS Publication, 298, p.32 - 42. ISBN 1-901502-23-6]</ref>.  Long-term performance studies have documented sustained removal of trichloroethene and [[Wikipedia: Hexavalent chromium | hexavalent chromium]] by ZVI PRBs and their continued hydraulic performance for up to 15 years<ref name= "Warner2005"/><ref>Phillips, D.H., Nooten, T.V., Bastiaens, L., Russell, M.I., Dickson, K., Plant, S., Ahad, J.M.E., Newton, T., Elliot, T. and Kalin, R.M., 2010. Ten year performance evaluation of a field-scale zero-valent iron permeable reactive barrier installed to remediate trichloroethene contaminated groundwater. Environmental Science & Technology, 44(10), pp.3861-3869. [https://doi.org/10.1021/es902737t doi: 10.1021/es902737t]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Puls, R.W., Lee, T.R. and Woods, L.L., 2014. Fifteen-year assessment of a permeable reactive barrier for treatment of chromate and trichloroethylene in groundwater. Science of the Total Environment, 468, pp.186-194. [https://doi.org/10.1016/j.scitotenv.2013.08.056 doi: 10.1016/j.scitotenv.2013.08.056]</ref>.
 {| class="wikitable" style="float: left; text-align: left; margin-right: 20px;"
@@ Line 47: / Line 49: @@
 | Metals || Lead <br />Cadmium <br />Nickel <br />Zinc <br />Mercury || Precipitation <br />Co-precipitation <br />Adsorption
 |}
 Zerovalent Iron has also been used in pilot or full-scale tests to treat groundwater contaminated with metals (e.g., chromium), metalloids (e.g., arsenic), and radionuclides (e.g., uranium)<ref>Blowes, D.W., Ptacek, C.J., Benner, S.G., McRae, C.W., Bennett, T.A. and Puls, R.W., 2000. Treatment of inorganic contaminants using permeable reactive barriers. Journal of Contaminant Hydrology, 45(1), pp.123-137</ref><ref>Puls, R.W., Paul, C.J. and Powell, R.M., 1999. The application of in situ permeable reactive (zero-valent iron) barrier technology for the remediation of chromate-contaminated groundwater: a field test. Applied Geochemistry, 14(8), pp.989-1000. [https://doi.org/10.1016/S0883-2927(99)00010-4 doi: 10.1016/s0883-2927(99)00010-4]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Beak, D.G. and Lee, T.R., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 1. Hydrogeochemical studies. Journal of Contaminant Hydrology, 106(1-2), pp.1-14. [https://doi.org/10.1016/j.jconhyd.2008.12.002 doi: 10.1016/j.jconhyd.2008.12.002]</ref><ref>Morrison, S.J., Metzler, D.R. and Carpenter, C.E., 2001. Uranium precipitation in a permeable reactive barrier by progressive irreversible dissolution of zerovalent iron. Environmental Science & Technology, 35(2), pp.385-390. [https://doi.org/10.1021/es001204i  doi: 10.1021/es001204i]</ref>.  Contaminant removal processes are complex and involve a combination of sorption to the surface of the ZVI or secondary minerals formed in the PRB, reductive precipitation, and co-precipitation. Other possible uses of ZVI for groundwater include treatment of explosives such as nitro aromatic compounds<ref>Agrawal, A. and Tratnyek, P.G., 1995. Reduction of nitro aromatic compounds by zero-valent iron metal. Environmental Science & Technology,30(1), pp.153-160. [http://dx.doi.org/10.1021/es950211h doi:10.1021/es950211h]</ref><ref>Scherer, M.M., Johnson, K.M., Westall, J.C. and Tratnyek, P.G., 2001. Mass transport effects on the kinetics of nitrobenzene reduction by iron metal. Environmental Science & Technology, 35(13), pp.2804-2811. [https://doi.org/10.1021/es0016856 doi: 10.1021/es0016856]</ref>.  Treatment applications of ZVI for organic and inorganic contaminants encountered in groundwater at hazardous waste sites are summarized in Table 1.

@@ Line 28: / Line 28: @@
 The first field-scale test of a PRB constructed with ZVI was conducted in 1991 at the Canadian Forces Base, Borden, Ontario by researchers from the University of Waterloo<ref>Gillham, R.W. and O'Hannesin, S.F., 1994. Enhanced degradation of halogenated aliphatics by zero‐valent iron. Groundwater, 32(6), pp.958-967. [https://doi.org/10.1111/j.1745-6584.1994.tb00935.x doi: 10.1111/j.1745-6584.1994.tb00935.x]</ref><ref>O'Hannesin, S.F. and Gillham, R.W., 1998. Long‐term performance of an in situ “iron wall” for remediation of VOCs. Groundwater, 36(1), pp.164-170. [https://doi.org/10.1111/j.1745-6584.1998.tb01077.x doi: 10.1111/j.1745-6584.1998.tb01077.x]</ref>.  The first full-scale ZVI-based PRB was constructed in Sunnyvale, California in 1994 to treat groundwater contaminated with TCE and ''cis''-DCE<ref name= "Warner2005">Warner, S.D., Longino, B.L., Zhang, M.I.A.O., Bennett, P., Szerdy, F.S. and Hamilton, L.A., 2005. The first commercial permeable reactive barrier composed of granular iron: hydraulic and chemical performance at 10 years of operation. IAHS Publication, 298, p.32 - 42. ISBN 1-901502-23-6]</ref>.  Long-term performance studies have documented sustained removal of trichloroethene and [[Wikipedia: Hexavalent chromium | hexavalent chromium]] by ZVI PRBs and their continued hydraulic performance for up to 15 years<ref name= "Warner2005"/><ref>Phillips, D.H., Nooten, T.V., Bastiaens, L., Russell, M.I., Dickson, K., Plant, S., Ahad, J.M.E., Newton, T., Elliot, T. and Kalin, R.M., 2010. Ten year performance evaluation of a field-scale zero-valent iron permeable reactive barrier installed to remediate trichloroethene contaminated groundwater. Environmental Science & Technology, 44(10), pp.3861-3869. [https://doi.org/10.1021/es902737t doi: 10.1021/es902737t]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Puls, R.W., Lee, T.R. and Woods, L.L., 2014. Fifteen-year assessment of a permeable reactive barrier for treatment of chromate and trichloroethylene in groundwater. Science of the Total Environment, 468, pp.186-194. [https://doi.org/10.1016/j.scitotenv.2013.08.056 doi: 10.1016/j.scitotenv.2013.08.056]</ref>.
-ZVI degrades chlorinated ethenes, ethanes, and methanes via reductive abiotic reactions that largely circumvent the production of toxic chlorinated daughter compounds, such as vinyl chloride, which can be produced during biological reduction<ref>Matheson, L.J. and Tratnyek, P.G., 1994. Reductive dehalogenation of chlorinated methanes by iron metal. Environmental Science & Technology, 28(12), pp.2045-2053. [http://dx.doi.org/10.1021/es00061a012 doi:10.1021/es00061a012]</ref><ref name= "Arnold2000">Arnold, W.A. and Roberts, A.L., 2000. Pathways and kinetics of chlorinated ethylene and chlorinated acetylene reaction with Fe (0) particles. Environmental Science & Technology, 34(9), pp.1794-1805. [https://doi.org/10.1021/es990884q doi: 10.1021/es990884q]</ref>.  For example, Arnold and Roberts<ref name= "Arnold2000"/> reported that >85% of PCE and >90% of TCE treatment by zerovalent iron is accounted for by [[Wikipedia: Elimination reaction | &beta;-elimination reactions]] that avoid production of ''cis''-DCE and VC.
+{| class="wikitable" style="float: left; text-align: left; margin-right: 20px;"
 |+ Table 1.  Groundwater Contaminants Treated by Granular ZVI
 |-
@@ Line 51: / Line 47: @@
 | Metals || Lead <br />Cadmium <br />Nickel <br />Zinc <br />Mercury || Precipitation <br />Co-precipitation <br />Adsorption
 |}
 ==PRB Design and Site Conditions==

@@ Line 54: / Line 54: @@
 ==PRB Design and Site Conditions==
 Like other ''in-situ'' technologies used for groundwater cleanup, PRB designs rely on accurate site characterization data for geology, hydrology, and groundwater geochemistry. Site hydrologic aspects critical for PRB design and performance include seasonal consistency in groundwater flow direction to maintain migration of contaminants to the PRB at an appropriate flow velocity. High flow velocities (≳2 m/d) can result in short residence time in the treatment zone and early breakthrough of contaminants; low flow velocities (≲0.1 m/d) result in little change in contaminant concentrations over time, so wells in down-gradient regions respond slowly.
-Geochemical considerations for the design of ZVI PRBs include redox conditions and the concentrations and make up of major ions dissolved in local groundwater. Geochemical conditions that are favorable for the sustained performance of ZVI PRBs include:
+Geochemical considerations for the design of ZVI PRBs include [[Wikipedia: Redox | redox]] conditions and the concentrations of major ions dissolved in local groundwater. Geochemical conditions that are favorable for the sustained performance of ZVI PRBs include:
-<u>Dissolved O<sub>2</sub> concentrations ≲2 mg/L</u>: Excess dissolved oxygen leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure.
+*<u>Dissolved O<sub>2</sub> concentrations ≲2 mg/L</u>: Excess dissolved oxygen leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure.
-<u>Nitrate-N concentrations ≲10 mg/L</u>: Like dissolved oxygen, nitrate enhanced iron corrosion leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure<ref>Liang, L., Moline, G.R., Kamolpornwijit, W. and West, O.R., 2005. Influence of hydrogeochemical processes on zero-valent iron reactive barrier performance: A field investigation. Journal of Contaminant Hydrology, 78(4), pp.291-312. [https://doi.org/10.1016/j.jconhyd.2005.05.006 doi: 10.1016/j.jconhyd.2005.05.006]</ref>.
+*<u>Nitrate-N concentrations ≲10 mg/L</u>: Like dissolved oxygen, nitrate enhanced iron corrosion leads to rapid iron corrosion and formation of low density iron oxide precipitates that may lead to hydraulic failure<ref>Liang, L., Moline, G.R., Kamolpornwijit, W. and West, O.R., 2005. Influence of hydrogeochemical processes on zero-valent iron reactive barrier performance: A field investigation. Journal of Contaminant Hydrology, 78(4), pp.291-312. [https://doi.org/10.1016/j.jconhyd.2005.05.006 doi: 10.1016/j.jconhyd.2005.05.006]</ref>.
-<u>Bicarbonate alkalinity ≲250 mg CaCO<sub>3</sub>/L</u>: Carbonate minerals (aragonite, siderite, chukanovite, carbonate-green rust) precipitate in the moderately alkaline pH environment (pH<sup>~</sup>10) produced by ZVI PRBs and most of the porosity and reactivity reduction in PRBs can be accounted for by these minerals (see Figure 2)<ref>Jeen, S.W., Gillham, R.W. and Blowes, D.W., 2006. Effects of carbonate precipitates on long-term performance of granular iron for reductive dechlorination of TCE. Environmental Science & Technology, 40(20), pp.6432-6437. [https://doi.org/10.1021/es0608747 doi: 10.1021/es0608747]</ref><ref>Li, L., Benson, C.H. and Lawson, E.M., 2006. Modeling porosity reductions caused by mineral fouling in continuous-wall permeable reactive barriers. Journal of Contaminant Hydrology, 83(1-2), pp.89-121. [https://doi.org/10.1016/j.jconhyd.2005.11.004 doi: 10.1016/j.jconhyd.2005.11.004]</ref><ref>Parbs, A., Ebert, M. and Dahmke, A., 2007. Long-term effects of dissolved carbonate species on the degradation of trichloroethylene by zerovalent iron. Environmental Science & Technology, 41(1), pp.291-296. [https://doi.org/10.1021/es061397v  doi: 10.1021/es061397v]</ref><ref>Henderson, A.D. and Demond, A.H., 2007. Long-term performance of zero-valent iron permeable reactive barriers: a critical review. Environmental Engineering Science, 24(4), pp.401-423. [https://doi.org/10.1089/ees.2006.0071 doi: 10.1089/ees.2006.0071]</ref>.
+*<u>Bicarbonate alkalinity ≲250 mg CaCO<sub>3</sub>/L</u>: Carbonate minerals (aragonite, siderite, chukanovite, carbonate-green rust) precipitate in the moderately alkaline pH environment (pH<sup>~</sup>10) produced by ZVI PRBs and most of the porosity and reactivity reduction in PRBs can be accounted for by these minerals (see Figure 2)<ref>Jeen, S.W., Gillham, R.W. and Blowes, D.W., 2006. Effects of carbonate precipitates on long-term performance of granular iron for reductive dechlorination of TCE. Environmental Science & Technology, 40(20), pp.6432-6437. [https://doi.org/10.1021/es0608747 doi: 10.1021/es0608747]</ref><ref>Li, L., Benson, C.H. and Lawson, E.M., 2006. Modeling porosity reductions caused by mineral fouling in continuous-wall permeable reactive barriers. Journal of Contaminant Hydrology, 83(1-2), pp.89-121. [https://doi.org/10.1016/j.jconhyd.2005.11.004 doi: 10.1016/j.jconhyd.2005.11.004]</ref><ref>Parbs, A., Ebert, M. and Dahmke, A., 2007. Long-term effects of dissolved carbonate species on the degradation of trichloroethylene by zerovalent iron. Environmental Science & Technology, 41(1), pp.291-296. [https://doi.org/10.1021/es061397v  doi: 10.1021/es061397v]</ref><ref>Henderson, A.D. and Demond, A.H., 2007. Long-term performance of zero-valent iron permeable reactive barriers: a critical review. Environmental Engineering Science, 24(4), pp.401-423. [https://doi.org/10.1089/ees.2006.0071 doi: 10.1089/ees.2006.0071]</ref>.
-<u>Sulfate concentrations ≳100 mg/L</u>: High dissolved hydrogen generated by iron corrosion creates a favorable environment for sulfate-reducing bacteria and methane-producing archaea. Metal sulfide precipitates like mackinawite (FeS) provide a source of secondary reactivity for chlorinated solvents and metals<ref>Butler, E.C. and Hayes, K.F., 1999. Kinetics of the transformation of trichloroethylene and tetrachloroethylene by iron sulfide. Environmental Science & Technology, 33(12), pp.2021-2027. [http://dx.doi.org/10.1021/es9809455 doi: 10.1021/es9809455]</ref><ref>Beak, D.G. and Wilkin, R.T., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 2. Geochemical modeling and solid phase studies. Journal of Contaminant Hydrology, 106(1-2), pp.15-28. [https://doi.org/10.1016/j.jconhyd.2008.12.003 doi: 10.1016/j.jconhyd.2008.12.003]</ref>.  Thus, levels of sulfate in influent groundwater promote natural sulfidation of ZVI PRBs and potentially enhanced treatment capacity<ref>Fan, D., Lan, Y., Tratnyek, P.G., Johnson, R.L., Filip, J., O’Carroll, D.M., Nunez Garcia, A. and Agrawal, A., 2017. Sulfidation of iron-based materials: A review of processes and implications for water treatment and remediation. Environmental Science & Technology, 51(22), pp.13070-13085. [https://doi.org/10.1021/acs.est.7b04177  doi: 10.1021/acs.est.7b04177]</ref>.
+*<u>Sulfate concentrations ≳100 mg/L</u>: High dissolved hydrogen generated by iron corrosion creates a favorable environment for sulfate-reducing bacteria and methane-producing archaea. Metal sulfide precipitates like mackinawite (FeS) provide a source of secondary reactivity for chlorinated solvents and metals<ref>Butler, E.C. and Hayes, K.F., 1999. Kinetics of the transformation of trichloroethylene and tetrachloroethylene by iron sulfide. Environmental Science & Technology, 33(12), pp.2021-2027. [http://dx.doi.org/10.1021/es9809455 doi: 10.1021/es9809455]</ref><ref>Beak, D.G. and Wilkin, R.T., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 2. Geochemical modeling and solid phase studies. Journal of Contaminant Hydrology, 106(1-2), pp.15-28. [https://doi.org/10.1016/j.jconhyd.2008.12.003 doi: 10.1016/j.jconhyd.2008.12.003]</ref>.  Thus, levels of sulfate in influent groundwater promote natural sulfidation of ZVI PRBs and potentially enhanced treatment capacity<ref>Fan, D., Lan, Y., Tratnyek, P.G., Johnson, R.L., Filip, J., O’Carroll, D.M., Nunez Garcia, A. and Agrawal, A., 2017. Sulfidation of iron-based materials: A review of processes and implications for water treatment and remediation. Environmental Science & Technology, 51(22), pp.13070-13085. [https://doi.org/10.1021/acs.est.7b04177  doi: 10.1021/acs.est.7b04177]</ref>.
-<u>Total dissolved solids below ≲1500 mg/L</u>:  The amount of secondary mineralization and clogging potential increases with increasing solute levels.
+*<u>Total dissolved solids below ≲1500 mg/L</u>:  The amount of secondary mineralization and clogging potential increases with increasing solute levels.
 [[File:Wilkin1w2 Fig2.png|thumb|Figure 2. False-color scanning electron micrograph<ref>ESTCP, 2018. Analysis of Long-Term Performance of Zero-valent Iron Applications. Project Report #ER-201589-PR. [[media:2018-ESTCP_Analysis_of_Long-Term_performance_of_Zero-valent_Iron_App.pdf| Report.pdf]]</ref> of a zero-valent iron grain (pink) coated with secondary precipitates (iron oxide and aragonite; green) surrounded by native aquifer quartz grains (blue). The iron particle is approximately 1.5 mm in length. ]]
@@ Line 71: / Line 71: @@
 Performance monitoring of PRBs typically includes: 1) sampling groundwater monitoring wells located up-gradient of the PRB to establish influent contaminant concentrations and groundwater geochemistry; 2) sampling groundwater monitoring wells located within the PRB to establish in-wall behavior; and, 3) sampling groundwater monitoring wells located down-gradient of the PRB to establish contaminant concentrations and groundwater geochemistry in the effluent. Key monitoring parameters include: contaminant(s) and daughter product(s), pH, oxidation-reduction potential, specific conductance, alkalinity, calcium, iron, and sulfate. These monitoring parameters provide an indication of whether or not the expected geochemical environment is present within the treatment zone, and also that contaminant degradation is occurring.
-For chlorinated solvents, analysis of the parent compounds and daughter products (e.g., ethene and ethane) aids in the performance analysis. Compound-specific isotope analysis can be helpful to understand contaminant degradation processes in complicated systems<ref>VanStone, N., Przepiora, A., Vogan, J., Lacrampe-Couloume, G., Powers, B., Perez, E., Mabury, S. and Lollar, B.S., 2005. Monitoring trichloroethene remediation at an iron permeable reactive barrier using stable carbon isotopic analysis. Journal of Contaminant Hydrology, 78(4), pp.313-325. [https://doi.org/10.1016/j.jconhyd.2005.05.013 doi: 10.1016/j.jconhyd.2005.05.013]</ref><ref>Lojkasek‐Lima, P., Aravena, R., Shouakar‐Stash, O., Frape, S.K., Marchesi, M., Fiorenza, S. and Vogan, J., 2012. Evaluating TCE abiotic and biotic degradation pathways in a permeable reactive barrier using compound specific isotope analysis. Groundwater Monitoring & Remediation, 32(4), pp.53-62. [https://doi.org/10.1111/j.1745-6592.2012.01403.x doi: 10.1111/j.1745-6592.2012.01403.x]</ref>.
+For chlorinated solvents, analysis of the parent compounds and daughter products (e.g., ethene and ethane) aids in the performance analysis. [[Compound Specific Isotope Analysis (CSIA)]] can be helpful to understand contaminant degradation processes in complicated systems<ref>VanStone, N., Przepiora, A., Vogan, J., Lacrampe-Couloume, G., Powers, B., Perez, E., Mabury, S. and Lollar, B.S., 2005. Monitoring trichloroethene remediation at an iron permeable reactive barrier using stable carbon isotopic analysis. Journal of Contaminant Hydrology, 78(4), pp.313-325. [https://doi.org/10.1016/j.jconhyd.2005.05.013 doi: 10.1016/j.jconhyd.2005.05.013]</ref><ref>Lojkasek‐Lima, P., Aravena, R., Shouakar‐Stash, O., Frape, S.K., Marchesi, M., Fiorenza, S. and Vogan, J., 2012. Evaluating TCE abiotic and biotic degradation pathways in a permeable reactive barrier using compound specific isotope analysis. Groundwater Monitoring & Remediation, 32(4), pp.53-62. [https://doi.org/10.1111/j.1745-6592.2012.01403.x doi: 10.1111/j.1745-6592.2012.01403.x]</ref>.
 Hydrologic monitoring typically consists of gradient analysis to determine flow directions and whether water level changes are abrupt in the vicinity of the PRB, indicating the potential for impeded groundwater flow. Core collection with solid-phase analysis and/or geophysical surveys (e.g., conductivity probing) are not common or routine components of performance monitoring, but can be considered in situations where anomalous behavior is encountered such as a failure to meet performance criteria.
-Problems noted with the application of this, and other, ''in situ''technologies include:
+Problems noted with the application of this, and other, ''in situ'' technologies include:
 *contaminants are present down-gradient of the PRB prior to installation;
 *influent contaminant concentrations may increase with time such that necessary residence time requirements are not met;

@@ Line 32: / Line 32: @@
 Zerovalent Iron has also been used in pilot or full-scale tests to treat groundwater contaminated with metals (e.g., chromium), metalloids (e.g., arsenic), and radionuclides (e.g., uranium)<ref>Blowes, D.W., Ptacek, C.J., Benner, S.G., McRae, C.W., Bennett, T.A. and Puls, R.W., 2000. Treatment of inorganic contaminants using permeable reactive barriers. Journal of Contaminant Hydrology, 45(1), pp.123-137</ref><ref>Puls, R.W., Paul, C.J. and Powell, R.M., 1999. The application of in situ permeable reactive (zero-valent iron) barrier technology for the remediation of chromate-contaminated groundwater: a field test. Applied Geochemistry, 14(8), pp.989-1000. [https://doi.org/10.1016/S0883-2927(99)00010-4 doi: 10.1016/s0883-2927(99)00010-4]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Beak, D.G. and Lee, T.R., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 1. Hydrogeochemical studies. Journal of Contaminant Hydrology, 106(1-2), pp.1-14. [https://doi.org/10.1016/j.jconhyd.2008.12.002 doi: 10.1016/j.jconhyd.2008.12.002]</ref><ref>Morrison, S.J., Metzler, D.R. and Carpenter, C.E., 2001. Uranium precipitation in a permeable reactive barrier by progressive irreversible dissolution of zerovalent iron. Environmental Science & Technology, 35(2), pp.385-390. [https://doi.org/10.1021/es001204i  doi: 10.1021/es001204i]</ref>.  Contaminant removal processes are complex and involve a combination of sorption to the surface of the ZVI or secondary minerals formed in the PRB, reductive precipitation, and co-precipitation. Other possible uses of ZVI for groundwater include treatment of explosives such as nitro aromatic compounds<ref>Agrawal, A. and Tratnyek, P.G., 1995. Reduction of nitro aromatic compounds by zero-valent iron metal. Environmental Science & Technology,30(1), pp.153-160. [http://dx.doi.org/10.1021/es950211h doi:10.1021/es950211h]</ref><ref>Scherer, M.M., Johnson, K.M., Westall, J.C. and Tratnyek, P.G., 2001. Mass transport effects on the kinetics of nitrobenzene reduction by iron metal. Environmental Science & Technology, 35(13), pp.2804-2811. [https://doi.org/10.1021/es0016856 doi: 10.1021/es0016856]</ref>.  Treatment applications of ZVI for organic and inorganic contaminants encountered in groundwater at hazardous waste sites are summarized in Table 1.
-{| class="wikitable" style="text-align: left;"
+{| class="wikitable" style="text-align: left; margin-left: auto; margin-right: auto;"
-{| class="wikitable" style="margin-left: auto; margin-right: auto; border: none;
+|+ Table 1.  Groundwater Contaminants Treated by Granular ZVI
 |-
 ! Contaminant Class

@@ Line 1: / Line 1: @@
-Permeable reactive barriers (PRBs) are ''in situ'' treatment zones created below ground to clean up contaminated groundwater. PRBs take advantage of natural groundwater migration to transport contaminants to a defined treatment zone. Contaminants are removed from groundwater in the PRB and treated groundwater passes through the permeable zone; eventually a “clean front” is created on the down-gradient side of the PRB.  Zerovalent Iron (ZVI) was the first reactive material used in PRBs for groundwater remediation and it continues to be the primary material used in the construction of these treatment systems. ZVI PRBs can treat groundwater contaminated with chlorinated solvents and their breakdown products such as tetrachloroethene (PCE), trichloroethene (TCE), ''cis''-1,2-dichloroethene (''cis''-DCE), vinyl chloride (VC), 1,1,1-trichloroethane (1,1,1-TCA), 1,1-dichloroethane (1,1-DCA), 1,2-dichloroethane (1,2-DCA), chloroform, and carbon tetrachloride; explosives such as TNT and RDX; cations of Pb, Cd, Ni, Zn, and Hg; and anions of Cr, As, Sb, Se, U, and Tc.
+Permeable reactive barriers (PRBs) are ''in situ'' treatment zones created below ground to clean up contaminated groundwater. PRBs take advantage of natural groundwater migration to transport contaminants to a defined treatment zone. Contaminants are removed from groundwater in the PRB as treated groundwater passes through the permeable zone. Eventually a “clean front” is created on the down-gradient side of the PRB.  [[Zerovalent Iron (ZVI) (Chemical Reduction - ISCR) | Zerovalent Iron (ZVI)]] was the first reactive material used in PRBs for groundwater remediation, and it continues to be the primary material used in the construction of these treatment systems. ZVI PRBs can treat groundwater contaminated with [[Chlorinated Solvents | chlorinated solvents]] and their breakdown products such as [[Wikipedia: Tetrachloroethylene | tetrachloroethene (PCE)]], [[Wikipedia: Trichloroethylene | trichloroethene (TCE)]], [[Wikipedia: 1,2-Dichloroethene |''cis''-1,2-dichloroethene (''cis''-DCE)]], [[Wikipedia: Vinyl chloride | vinyl chloride (VC)]], [[Wikipedia: 1,1,1-Trichloroethane | 1,1,1-trichloroethane (1,1,1-TCA)]], [[Wikipedia: 1,1-Dichloroethane | 1,1-dichloroethane (1,1-DCA)]], [[Wikipedia: 1,2-Dichloroethane | 1,2-dichloroethane (1,2-DCA)]], [[Wikipedia: Chloroform | chloroform]], and [[Wikipedia: Carbon tetrachloride | carbon tetrachloride]]; also explosives such as [[Wikipedia: TNT | TNT]] and [[Wikipedia: RDX | RDX]]; as well as cations of Pb, Cd, Ni, Zn, and Hg; and anions of Cr, As, Sb, Se, U, and Tc.
 <div style="float:right;margin:0 0 2em 2em;">__TOC__</div>
@@ Line 18: / Line 18: @@
 ==Introduction==
-A PRB is commonly constructed using granular iron, limestone, organic-carbon, zeolites, apatite, or mixtures of these materials with sand or gravel<ref name= "ITRC2005W"/><ref name= "ITRC2011W"/>.  PRBs are installed hydraulically down-gradient from contaminant source zones to prevent off-site plume migration or to protect sensitive receptors. Design considerations for PRBs include:
+A PRB is commonly constructed using granular iron, limestone, organic-carbon, [[Wikipedia: Zeolite | zeolites]], [[Wikipedia: Apatite | apatite]], or mixtures of these materials with sand or gravel<ref name= "ITRC2005W"/><ref name= "ITRC2011W"/>.  PRBs are installed hydraulically down-gradient from contaminant source zones to prevent off-site plume migration or to protect sensitive receptors. Design considerations for PRBs include:
 #understanding contaminant flux to determine the residence time requirement for effective treatment;
 #understanding geochemical conditions to identify compatibility issues between the selected reactive medium and site-specific groundwater; and
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 ==Zerovalent Iron==
-The first field-scale test of a PRB constructed with ZVI was conducted in 1991 at the Canadian Forces Base, Borden, Ontario by researchers from the University of Waterloo<ref>Gillham, R.W. and O'Hannesin, S.F., 1994. Enhanced degradation of halogenated aliphatics by zero‐valent iron. Groundwater, 32(6), pp.958-967. [https://doi.org/10.1111/j.1745-6584.1994.tb00935.x doi: 10.1111/j.1745-6584.1994.tb00935.x]</ref><ref>O'Hannesin, S.F. and Gillham, R.W., 1998. Long‐term performance of an in situ “iron wall” for remediation of VOCs. Groundwater, 36(1), pp.164-170. [https://doi.org/10.1111/j.1745-6584.1998.tb01077.x doi: 10.1111/j.1745-6584.1998.tb01077.x]</ref>.  The first full-scale ZVI-based PRB was constructed in Sunnyvale, California in 1994 to treat groundwater contaminated with TCE and ''cis''-DCE<ref name= "Warner2005">Warner, S.D., Longino, B.L., Zhang, M.I.A.O., Bennett, P., Szerdy, F.S. and Hamilton, L.A., 2005. The first commercial permeable reactive barrier composed of granular iron: hydraulic and chemical performance at 10 years of operation. IAHS Publication, 298, p.32 - 42. ISBN 1-901502-23-6]</ref>.  Long-term performance studies have documented sustained removal of trichloroethene and hexavalent chromium by ZVI PRBs and their continued hydraulic performance for up to 15 years<ref name= "Warner2005"/><ref>Phillips, D.H., Nooten, T.V., Bastiaens, L., Russell, M.I., Dickson, K., Plant, S., Ahad, J.M.E., Newton, T., Elliot, T. and Kalin, R.M., 2010. Ten year performance evaluation of a field-scale zero-valent iron permeable reactive barrier installed to remediate trichloroethene contaminated groundwater. Environmental Science & Technology, 44(10), pp.3861-3869. [https://doi.org/10.1021/es902737t doi: 10.1021/es902737t]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Puls, R.W., Lee, T.R. and Woods, L.L., 2014. Fifteen-year assessment of a permeable reactive barrier for treatment of chromate and trichloroethylene in groundwater. Science of the Total Environment, 468, pp.186-194. [https://doi.org/10.1016/j.scitotenv.2013.08.056 doi: 10.1016/j.scitotenv.2013.08.056]</ref>.
+The first field-scale test of a PRB constructed with ZVI was conducted in 1991 at the Canadian Forces Base, Borden, Ontario by researchers from the University of Waterloo<ref>Gillham, R.W. and O'Hannesin, S.F., 1994. Enhanced degradation of halogenated aliphatics by zero‐valent iron. Groundwater, 32(6), pp.958-967. [https://doi.org/10.1111/j.1745-6584.1994.tb00935.x doi: 10.1111/j.1745-6584.1994.tb00935.x]</ref><ref>O'Hannesin, S.F. and Gillham, R.W., 1998. Long‐term performance of an in situ “iron wall” for remediation of VOCs. Groundwater, 36(1), pp.164-170. [https://doi.org/10.1111/j.1745-6584.1998.tb01077.x doi: 10.1111/j.1745-6584.1998.tb01077.x]</ref>.  The first full-scale ZVI-based PRB was constructed in Sunnyvale, California in 1994 to treat groundwater contaminated with TCE and ''cis''-DCE<ref name= "Warner2005">Warner, S.D., Longino, B.L., Zhang, M.I.A.O., Bennett, P., Szerdy, F.S. and Hamilton, L.A., 2005. The first commercial permeable reactive barrier composed of granular iron: hydraulic and chemical performance at 10 years of operation. IAHS Publication, 298, p.32 - 42. ISBN 1-901502-23-6]</ref>.  Long-term performance studies have documented sustained removal of trichloroethene and [[Wikipedia: Hexavalent chromium | hexavalent chromium]] by ZVI PRBs and their continued hydraulic performance for up to 15 years<ref name= "Warner2005"/><ref>Phillips, D.H., Nooten, T.V., Bastiaens, L., Russell, M.I., Dickson, K., Plant, S., Ahad, J.M.E., Newton, T., Elliot, T. and Kalin, R.M., 2010. Ten year performance evaluation of a field-scale zero-valent iron permeable reactive barrier installed to remediate trichloroethene contaminated groundwater. Environmental Science & Technology, 44(10), pp.3861-3869. [https://doi.org/10.1021/es902737t doi: 10.1021/es902737t]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Puls, R.W., Lee, T.R. and Woods, L.L., 2014. Fifteen-year assessment of a permeable reactive barrier for treatment of chromate and trichloroethylene in groundwater. Science of the Total Environment, 468, pp.186-194. [https://doi.org/10.1016/j.scitotenv.2013.08.056 doi: 10.1016/j.scitotenv.2013.08.056]</ref>.
-ZVI degrades chlorinated ethenes, ethanes, and methanes via reductive abiotic reactions that largely circumvent the production of toxic chlorinated daughter compounds, such as vinyl chloride, which can be produced during biological reduction<ref>Matheson, L.J. and Tratnyek, P.G., 1994. Reductive dehalogenation of chlorinated methanes by iron metal. Environmental Science & Technology, 28(12), pp.2045-2053. [http://dx.doi.org/10.1021/es00061a012 doi:10.1021/es00061a012]</ref><ref name= "Arnold2000">Arnold, W.A. and Roberts, A.L., 2000. Pathways and kinetics of chlorinated ethylene and chlorinated acetylene reaction with Fe (0) particles. Environmental Science & Technology, 34(9), pp.1794-1805. [https://doi.org/10.1021/es990884q doi: 10.1021/es990884q]</ref>.  For example, Arnold and Roberts<ref name= "Arnold2000"/> reported that >85% of PCE and >90% of TCE treatment by zerovalent iron is accounted for by &beta;-elimination reactions that avoid production of ''cis''-DCE and VC.
+ZVI degrades chlorinated ethenes, ethanes, and methanes via reductive abiotic reactions that largely circumvent the production of toxic chlorinated daughter compounds, such as vinyl chloride, which can be produced during biological reduction<ref>Matheson, L.J. and Tratnyek, P.G., 1994. Reductive dehalogenation of chlorinated methanes by iron metal. Environmental Science & Technology, 28(12), pp.2045-2053. [http://dx.doi.org/10.1021/es00061a012 doi:10.1021/es00061a012]</ref><ref name= "Arnold2000">Arnold, W.A. and Roberts, A.L., 2000. Pathways and kinetics of chlorinated ethylene and chlorinated acetylene reaction with Fe (0) particles. Environmental Science & Technology, 34(9), pp.1794-1805. [https://doi.org/10.1021/es990884q doi: 10.1021/es990884q]</ref>.  For example, Arnold and Roberts<ref name= "Arnold2000"/> reported that >85% of PCE and >90% of TCE treatment by zerovalent iron is accounted for by [[Wikipedia: Elimination reaction | &beta;-elimination reactions]] that avoid production of ''cis''-DCE and VC.
 Zerovalent Iron has also been used in pilot or full-scale tests to treat groundwater contaminated with metals (e.g., chromium), metalloids (e.g., arsenic), and radionuclides (e.g., uranium)<ref>Blowes, D.W., Ptacek, C.J., Benner, S.G., McRae, C.W., Bennett, T.A. and Puls, R.W., 2000. Treatment of inorganic contaminants using permeable reactive barriers. Journal of Contaminant Hydrology, 45(1), pp.123-137</ref><ref>Puls, R.W., Paul, C.J. and Powell, R.M., 1999. The application of in situ permeable reactive (zero-valent iron) barrier technology for the remediation of chromate-contaminated groundwater: a field test. Applied Geochemistry, 14(8), pp.989-1000. [https://doi.org/10.1016/S0883-2927(99)00010-4 doi: 10.1016/s0883-2927(99)00010-4]</ref><ref>Wilkin, R.T., Acree, S.D., Ross, R.R., Beak, D.G. and Lee, T.R., 2009. Performance of a zerovalent iron reactive barrier for the treatment of arsenic in groundwater: Part 1. Hydrogeochemical studies. Journal of Contaminant Hydrology, 106(1-2), pp.1-14. [https://doi.org/10.1016/j.jconhyd.2008.12.002 doi: 10.1016/j.jconhyd.2008.12.002]</ref><ref>Morrison, S.J., Metzler, D.R. and Carpenter, C.E., 2001. Uranium precipitation in a permeable reactive barrier by progressive irreversible dissolution of zerovalent iron. Environmental Science & Technology, 35(2), pp.385-390. [https://doi.org/10.1021/es001204i  doi: 10.1021/es001204i]</ref>.  Contaminant removal processes are complex and involve a combination of sorption to the surface of the ZVI or secondary minerals formed in the PRB, reductive precipitation, and co-precipitation. Other possible uses of ZVI for groundwater include treatment of explosives such as nitro aromatic compounds<ref>Agrawal, A. and Tratnyek, P.G., 1995. Reduction of nitro aromatic compounds by zero-valent iron metal. Environmental Science & Technology,30(1), pp.153-160. [http://dx.doi.org/10.1021/es950211h doi:10.1021/es950211h]</ref><ref>Scherer, M.M., Johnson, K.M., Westall, J.C. and Tratnyek, P.G., 2001. Mass transport effects on the kinetics of nitrobenzene reduction by iron metal. Environmental Science & Technology, 35(13), pp.2804-2811. [https://doi.org/10.1021/es0016856 doi: 10.1021/es0016856]</ref>.  Treatment applications of ZVI for organic and inorganic contaminants encountered in groundwater at hazardous waste sites are summarized in Table 1.

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 <div style="float:right;margin:0 0 2em 2em;">__TOC__</div>
 '''Related Article(s):'''
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 *[[Metal and Metalloids - Remediation]]
 *[[Chlorinated Solvents]]
 '''CONTRIBUTOR(S):''' [[Dr. Richard Wilkin]]

← Older revision		Revision as of 20:19, 23 January 2019
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	*[[Chlorinated Solvents]]		*[[Chlorinated Solvents]]

−	'''CONTRIBUTOR(S):'''	+	'''CONTRIBUTOR(S):''' [[Dr. Richard Wilkin]]