Engineered passive bioreactive barriers: risk-managing the legacy of industrial soil and groundwater pollution Robert M Kalin Permeable reactive barriers are a technology that is one decade old, with most full-scale applications based on abiotic mechanisms. Though there is extensive literature on engineered bioreactors, natural biodegradation potential, and in situ remediation, it is only recently that engineered passive bioreactive barrier technology is being considered at the commercial scale to manage contaminated soil and groundwater risks. Recent full-scale studies are providing the scientific confidence in our understanding of coupled microbial (and genetic), hydrogeologic, and geochemical processes in this approach and have highlighted the need to further integrate engineering and science tools. Addresses Environmental Engineering Research Centre, School of Civil Engineering, The Queen’s University of Belfast, Belfast BT9 5AG, Northern Ireland, UK e-mail: r.kalin@qub.ac.uk Current Opinion in Microbiology 2004, 7:227–238 This review comes from a themed issue on Ecology and industrial microbiology Edited by Elizabeth Wellington and Mike Larkin Available online 10th May 2004 1369-5274/$ – see front matter ß 2004 Elsevier Ltd. All rights reserved. DOI 10.1016/j.mib.2004.04.014 Abbreviations MNA monitored natural attenuation NA natural attenuation PRB permeable reactive barrier ‘Environmental Engineering is the integration of the built environment within the natural environment using science and engineering to meet the principles of social, economic and environmental sustainability’ Prof. Robert M. Kalin There are three primary strategies used separately or in conjunction to reduce or eliminate the risk of contaminants in soil and groundwater: 1. Destruction or alteration of contaminants. 2. Extraction or separation of contaminants from environmental media. 3. Immobilization of contaminants. There is a variety of both in situ and ex situ treatment technologies capable of contaminant destruction by altering the chemical structure including thermal, biological and chemical treatment methods. Highly engineered treatment technologies that are commonly used for extraction and separation of contaminants from environmental media include soil treatment by thermal desorption, soil washing, solvent extraction, soil vapour extraction and ground water treatment by either phase separation, carbon adsorption, air stripping, ion exchange, or by some combination of these technologies. Immobilization technologies are generally only applied to soilbased contamination and include stabilization, solidification and containment technologies, such as placement in a secure landfill or construction of cement-bentonite slurry walls. However, the contaminants have not been treated and it is now realized that no immobilization technology is permanently effective. The development of our current societal infrastructure and standard of living has produced a legacy of land and groundwater that is contaminated with potentially harmful inorganic and organic compounds. At the turn of the new millennium much of the developed world turned its attention to ‘sustainability’ where emphasis is now placed on a balance between economic, social and environmental issues. This change in emphasis on integration of the natural and anthropogenic environments is summarized in the following two quoted mission statements: To this end, it has been realized over the past three decades of environmental remediation that it is not possible to use engineering to completely degrade all contaminants that have been released to the environment. Thus, the development of remediation technologies to degrade these compounds has moved from strongly intensive in situ and ex situ treatments to combined engineered and passive/natural approaches (treatment train) that manage the risks associated with the ‘source’ of the contaminants, the ‘pathways’ of flux and contaminant transport and impact on the ‘receptor’ which may either be human health related or additional environmental impact. ‘We will be recognized as the leading source of knowledge and skills required to create a sustainable natural and built environment for the benefit of future generations’ Institution of Civil Engineers (ICE) UK Vision Statement One of the main obstacles to implementation of this ‘sustainable’ approach to dealing with contaminants in soil and groundwater is the added costs, in time and money, required to manage the risks of contaminants Introduction www.sciencedirect.com Current Opinion in Microbiology 2004, 7:227–238 228 Ecology and industrial microbiology in the environment. As a generalisation, the dominant ex situ method for dealing with contaminated soil has involved digging up much of the contamination and disposing it in landfills. However, both legislative pressure and the increased costs of land-filling (both in the UK, the EU and other countries) and a world-wide move towards more sustainable remedial technologies are prompting developers to consider alternative in situ and ex situ methods of dealing with organic contaminants. Alternative remediation technologies that permanently destroy or detoxify contaminants are becoming commonplace in the USA, Australasia and European countries. natural carbon substrates. Other complicating factors whereby natural degradative processes are limited include nutrient availability, redox conditions, substrate competition, bioavailability, toxicity and a combination of geologic, geotechnical and hydrogeologic factors that make the subsurface an immensely complex environment. An evolution of approach is needed which develops a conceptual understanding of all elements and identifies knowledge gaps. There is also a need for further development/refinement of tools for site study that will provide an understanding of the rate controlling mechanisms for natural biodegradative processes [23–25]. The complete degradation of man-made or xenobiotic chemicals by microorganisms in the environment is universally considered to be beneficial. In particular, those high priority pollutants of soils and groundwater’s that are regarded as carcinogenic and toxic (EU Council Directive 2000/60/EC). The concept of ‘microbial infallibility’ with respect to biodegradation has long been the assumption. Indeed, Stanley Dagley concluded in his introduction to the text ‘Microbial Degradation of Organic Compounds’ that ‘On thermodynamic grounds, no organic compound can be excluded from serving as a possible energy source for aerobic microorganisms’. In this review, I have chosen to write from the ‘engineering’ perspective and briefly touch upon a wide range of both engineering and science issues that must be considered for implementation of passive bioreactive barrier technology. This includes not only the microbiological biotransformations, but also where the technology has come from (including abiotic transformations), the wide scope of issues that are needed to design the engineering of a bioreactor that must operate with little or no maintenance for decades, and cost effective and rapid ways of monitoring the ‘health’ of the system. Engineered passive bioreactive barriers Some of the most promising alternative technologies are based therefore on bioremediation [1–3]. When considered from an ‘engineering’ perspective, there are two general approaches to microbial biodegradation i) those that use engineered or inoculated microorganisms [4–6], or ii) those that use natural microbial biodegrative potential [7–17,1819] in technologies such as bio-sparging, bio-slurping and natural attenuation (NA) [20–22]. Of these biological technologies, NA has received significant attention. NA relies on the indigenous microbial population and aquifer nutrients to biodegrade contaminants. Monitored natural attenuation (MNA) can be used for risk management and as a remediation method for contaminant plumes. The application of MNA can be limited by nutrient availability and/or high risks associated with contaminant movement, hence at some sites the potential to use NA as a risk management strategy is poor and intervention is necessary. There is a plethora of publications in the literature that describe microbial species, populations and mechanisms for biotransformation of potentially hazardous compounds, but many of these publications focus on a very limited number of substrates. ‘Real’ sites may have many hundreds or thousands of contaminants partitioned between soil, water and vapour phases, and for which bioremediation is expected to provide a successful reduction in risk. Engineering a sustainable bioremediation solution depends on long-term microbial populations that will biotransform a significant number of contaminant substrates and metabolites as well as a superfluity of Current Opinion in Microbiology 2004, 7:227–238 Permeable reactive barriers (PRBs) are a passive intervention remediation technology [26–31] that have been used for risk-management in even the most extreme environments found on earth [32,33,34,35,36]. In PRB systems contaminated groundwater passes through an in situ reactive material that either biotically or abiotically degrades the contaminants. PRBs are unique because they can be engineered to prevent contaminant movement across site boundaries before risk receptors, or simply to cut-off the source of a contaminant plume that then dissipates via NA processes. By far the most successful PRB technology to date is barriers of zero-valent iron [37–43,44,45]. The laboratory, pilot scale and full-scale experience, of which there are nearly 80 installations world-wide, have been shown to abiotically degrade chlorinated solvents such as trichloroethene and tetrachloroethene, trace metals and radionuclides, and inorganic contaminants such as nitrate and sulphate/sulphide [46–56]. Microorganisms have a greater scope for transformation of a wide range of compounds and recent studies are examining synergetic degradation between abiotic zero-valent iron and biologic processes [57,58]. There is a considerable research effort to continually find new abiotic methods for destruction of contaminants using passive techniques [59–61,62,63]. PRBs using activated carbon can remove many organic contaminants from groundwater through sorption (non-destructive process), but some compounds may not be removed, or if inappropriately designed, the effect of ‘roll-up’ may end in chromatographic effects that release concentrations of www.sciencedirect.com Engineered passive bioreactive barriers: risk-managing the legacy of industrial soil and groundwater pollution Kalin 229 contaminants in higher concentration than was originally observed [64–67,68,69,70,71]. tion of contaminated soil and groundwater for most compounds of concern [91–103,104,105,106,107]. The recent advancement on this technology is to use engineered passive bioreactors in situ to take advantage of the potential for microbial biotransformation of potentially hazardous compounds. Bioreactive ‘zones’ have been engineered to change redox conditions or provide substrates/nutrient that facilitate the natural biodegradative system [72–81]. Current biological reactive zones rely on either dissolved nutrients or injected nutrients to support the biodegradation of contaminants passing through the ‘barrier’. Delivery of nutrients throughout a barrier has been shown to be hydrologically difficult and can add considerable expense to a remediation project. Additionally, there is the potential that media must be replenished periodically. The engineering challenge was therefore to take existing knowledge and expertise and apply it passively using only the inertia of natural groundwater systems to transport a flux through the bioreactive barrier, and design systems capable of operation for years to decades with little or no maintenance. The overall performance of a bioreactive PRB must also balance the rate of contaminant degradation with the flux of contaminants entering the reactive zone. Laboratory batch and column studies using real site water and microbial populations can provide an estimate of the rate of biotransformation [108–112,113,114,115, 116,117]. However, there are a large number of variables that could be examined and it often takes significant research to elucidate the major factor(s) that control the occurrence and rate of biodegradation. Figure 1 presents a flow diagram of the decision making and design process for implementation of a PRB. An integral part of evaluation is laboratory and pilot scale experiments that study, under site conditions, the operational windows for in situ bioreactive barrier methods [118–121,122] before Given the complexity of the subsurface, passive bioreactive barriers have applied the principles and knowledge used in the biotransformation of potentially hazardous compounds with bioreactor technology [82–89,90]. Ex situ bioreactors have been used successfully for remedia- Figure 1 Risk assessment Solution identification Site investigation Hydrogeology Flux Biogeochemistry Microbiology Identification of knowledge gap Pilot scale trial studies Microbiology Geochemistry Evaluation of pilot scale Modelling Design and implementation Scale up to design criteria Engineering Evaluation Full scale PRB evaluation Evaluation Microbiology Geochemistry Current Opinion in Microbiology In situ passive remediation of contaminants in soil and groundwater (e.g. Permeable Reactive Barrier, PRB) must integrate the rate flux of substrate transport or availability, rates of natural or enhanced biodegradation with evaluation of the temporal uncertainty in each of these parameters to allow design and implementation. It will be essential that large complex genetic databases are easily available (at minimal cost) so that the emerging array technology can reach its ultimate potential and provide rapid and detailed feedback for remediation science and technology. www.sciencedirect.com Current Opinion in Microbiology 2004, 7:227–238 230 Ecology and industrial microbiology design and full-scale implementation of bioreactive PRB systems [123–132,133,134,135,136]. One of the most significant single-use sources of contaminated soil and groundwater in the UK and Europe is former coal gasification sites. The long and complex history of these activities has resulted in a wide range of compounds in soil and groundwater that require risk-management. There is a significant body of literature on the biotransformation of many of these compounds [137,138,139– 141], the use of ex situ bioreactor techniques [142–144] and recent applications of pilot-scale to full-scale PRBs for risk management of these sites [145–151]. Significant collaborative research on full-scale engineered bioreactive barrier systems at two UK Sites is on-going between two research groups at the Queen’s University Belfast (QUESTOR Centre and Environmental Engineering Research Centre), Oxford University and the University of Surrey, and two industrial partners, Second-Site Property Holding Ltd, and Parsons Brinkerhoff. Figure 2 shows the site and bioreactor layout for one of the projects on Sequential REactive BARrier (SEREBAR) remediation of contaminated groundwater, the results of this research has highlighted the need for integration of science and engineering when implementing this technology. Of particular note is the difficulty for prediction of not only how a bioactive barrier might adapt and function over timescales that range from days to decades, but also how to measure temporal changes in microbial populations. Figure 3 depicts a conceptual/hypothetical series of changes in microbial ecology or genetic diversity over time or resulting from shocks to the bioreactive barrier. Chemical monitoring of the system provides confirmatory cause/effect information on the end-result of biotransformation, or lack thereof, but can provide little predictive Figure 2 SEquenced REactive BARrier (SEREBAR) Abiotic Anaerobic Aerobic Sorptive Current Opinion in Microbiology Site and design drawings of the engineered bioreactive barrier for project SEREBAR at a former coal gasification site in the UK combining site groundwater flow and contaminant flux with abiotic, anaerobic biotransformation, aerobic biotransformation and abiotic sorption stages. Current Opinion in Microbiology 2004, 7:227–238 www.sciencedirect.com Engineered passive bioreactive barriers: risk-managing the legacy of industrial soil and groundwater pollution Kalin 231 Figure 3 Declining diversity Increasing microbial diversity or degradation potential Increasing diversity Adaptive diversity Toxic event Toxic event Toxic event Adaptive Biofilm Toxic event Biofilm not affected Biofilm strongly affected 0 5 10 15 Time (months) 20 25 30 Current Opinion in Microbiology In situ passive treatment of groundwater and soil is a process that takes months to decades and there is a lack of extant knowledge vis-à-vis the long-term response of microbial biodegradation on these time scales. There are several potential changes in microbial biodegradative potential over time, hypothetical variations shown here, which must be evaluated by the emerging body of research into this technology (e.g. the UK BBSRC Link and CLAIRE project SEREBAR). Note: A toxic event may reflect an abrupt change in substrate, nutrients or concentration. measure of the ‘health’ or ‘sustainability’ of the microbial populations doing all the work. There is a challenge to find cost effective and time efficient ways to monitor these systems at the biofilm/ microbiological level. On-line automated measurement is needed of toxicity, respiration, identification of metabolites, and potentially, direct methods [152–161,162]. The increasing use of isotopes, either natural abundance or labelled compounds provides direct evidence of substrate Table 1 Typical time frames for PRB implementation. Task Timeframe Technology selection Preliminary site evaluation and risk assessment Hydrogeologic study Detailed biogeochemical site evaluation Choice of technology generally 4 to 26 weeks 1 to 12 weeks 4 to 26 weeks 4 to 12 weeksa PRB remediation validation Hydrogeologic/contaminant flux modelling Laboratory trials/kinetics of reactions Conceptual design Pilot scale studies and conceptual design period generally 5 to 19 weeks 2 to 12 weeks 5 to 15 weeksa 2 to 4 weeks PRB tender and construction Engineering design Implementation/construction Engineering design and implementation generally 14 to 30 weeks 2 to 4 weeks 10 to 26 weeks PRB operation Monitoring and maintenance Years to decades In general, is takes between 6 months and 1.5 years for implementation of passive PRB technology. aHowever, there is a limited window of opportunity during which detailed microbial evaluation and results are able to provide specific design parameters. It is imperative that the microbial genetics revolution develops a capability to provide detailed understanding of both site investigation soil and groundwater samples and laboratory trials in a highly time efficient manner if this data are to be used in Engineering Design to its greatest potential. www.sciencedirect.com Current Opinion in Microbiology 2004, 7:227–238 232 Ecology and industrial microbiology utilization [162,163–167,168]. However, the greatest potential lies with array techniques that elucidate large amounts of genetic information on both expression and potential of the microbial community [169–175,176, 177]. The challenge will be providing a rapid, cost effective routine and reliable monitoring application of this technology. In particular, there is need to model the short-term and long-term behavior of engineered passive systems. A significant research effort is needed to couple predictive modeling of microbial behavior [178,179,180, 181,182], microbial transport and establishment within the bioreactor [182,183–188,189], the formation and behavior of the resulting biofilm [190–193] within the predictive design and modeling of full-scale PRB systems [194–201], and the response of bioremediation to changes in operational parameters [202–204]. A further challenge is to provide this information within a ‘typical’ project management time-line for an engineered PRB system such that the information can play a crucial role in the conceptual model, design and implementation. Table 1 presents recent experience on the evaluation, design and implementation of engineered bioreactive PRBs and the associated time-scales for sites in the UK. There is often only a matter of weeks during which sample collection, microbial evaluation and substrate utilization, and predictive study can take place. For detailed design, the results of microbial investigation must also be interpreted side-by-side with hydrogeological, biogeochemical and engineering results. Without readily available rapid and robust (inclusive and dependable) screening methods, there will continue to be a limited ability for detailed microbiological study to provide predictive design input for full-scale engineering, and thereby have the greatest benefit for implementation and monitoring of novel ‘sustainable’ technology. Conclusions Sustainability, economic, social and environmental, requires implementation of contaminated land and groundwater risk-management on decadal time scales. Although significant scientific understanding of natural bioattenuative processes has emerged, there is a current lack of knowledge or engineering experience that allows the accurate prediction of the long-term sustainability of passive engineered bioremediation systems for soil and groundwater. The challenge for the future is to use the potential of emerging microbial genetic methods to provide a prediction of long-term changes in microbial biodegradative potential in combination with hydrogeological, biogeochemical, geotechnical and engineering understanding for effective design and implementation. Acknowledgements The author would like to acknowledge years of discussion and research with collaborators at QUB and in the QUESTOR Centre, in particular Mike Larkin, at Oxford University, at the University of Surrey, in particular Stephan Jefferis, and members of PRB-Net, in particular Robert Puls Current Opinion in Microbiology 2004, 7:227–238 of the US EPA. The research experience of the author has been supported by the BBSRC, EPSRC, NERC, EA, and by industrial partners/collaborators, in particular the QUESTOR Industrial Board, Second-Site Property Holdings Ltd, Keller Ground Engineering, and Environmental Technologies (ETI). 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This is another paper on new media for permeable reactive barriers, however not only do the authors use laboratory columns, but they also use geochemical models to provide a validation and predictive element to the work. 71. Wan M-W, Petrisor IG, Lai H-T, Kim D, Yen TF: Copper adsorption through chitosan immobilized on sand to demonstrate the feasibility for in situ soil decontamination. Carbohydr Polym 2004, 55:249-254. This paper is representative of a body of literature in the civil and chemical engineering field where by-products of food engineering (in this case chitin) are proposed for full-scale permeable reactive barrier (PRB) applications. There is a need to bring this work together with microbial processes if the long-term sustainability of easily biodegradable material is to be used for long-term sorption PRBs. 72. Rijnaarts HHM, Hesselink PGM, Doddema HJ: Activated in situ bioscreens. In Contaminated Soil, vol 2. Edited by van den Brink WJ et al. 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Brough MJ, Al-Tabbaa A, Martin RJ: Active biofilm barriers for waste containment and bioremediation: laboratory assessment. Proceedings of the 4th International In Situ and On-Site Bioremediation Symposium 1997, 4:233-238. 61. Johnson JG, Odencrantz JE: Management of a hydrocarbon plume using a permeable ORC Barrier. Proceedings of the 4th International In Situ and On-Site Bioremediation Symposium 1997, 4:215-220. 62. Centi G, Perathoner S: Remediation of water contamination using catalytic technologies. Appl Catal Environ 2003, 1-2:15-29. This paper discusses how abiotic catalytic degradation could be used for methyl tertiary butyl ether and other contaminants, and interestingly suggests that microbiological breakdown of residual compounds is expected at the back end of the process. 63. Bill M, Schüth C, Barth JAC, Kalin RM: Carbon isotope fractionation during abiotic reductive dehalogenation of trichloroethene (TCE). Chemosphere 2001, 44:1281-1286. 64. Smith CC, Anderson WF, Freewood RJ: Evaluation of shredded tyre chips as sorption media for passive treatment walls. Eng Geol 2001, 1-4:253-261. 65. Lorbeer H, Starke S, Gozan M, Tiehm A, Werner P: Bioremediation of chlorobenzene-contaminated groundwater on granular activated carbon barriers, water, air and soil pollution. Focus 2002, 2:183-193. 77. Hunkeler D, Höhener P, Bernasconi S, Zeyer J: Engineered in situ bioremediation of a petroleum hydrocarbon-contaminated aquifer: assessment of mineralization based on alkalinity, inorganic carbon and stable carbon isotope balances. J Contam Hydrol 1999, 37:201-223. 78. Barbaro JR, Barker JF: Controlled field study on the use of nitrate and oxygen for bioremediation of a gasoline source zone. Bioremediation J 2000, 4:259-270. 79. Hunkeler D, Höhener P, Zeyer J: Engineered and subsequent intrinsic in situ bioremediation of a diesel fuel contaminated aquifer. J Contam Hydrol 2002, 59:231-245. 80. Fang Y, Hozalski RM, Clapp LW, Novak PJ, Semmens MJ: Passive dissolution of hydrogen gas into groundwater using hollow-fiber membranes. Water Res 2002, 36:3533-3542. 81. Witt MlE, Klecka GM, Lutz EJ, Ei TA, Grosso NR, Chapelle FH: Natural attenuation of chlorinated solvents at Area 6, Dover Air Force Base: groundwater biogeochemistry. J Contam Hydrol 2002, 57:61-80. 66. Czurda KA, Haus R: Reactive barriers with fly ash zeolites for in situ groundwater remediation. Appl Clay Sci 2002, 1-2:13-20. 82. Jacobsen BN, Becher G, Jensen BK, Monarca S, ScholzMuramatsu H, Struijs J: Fate prediction of specific organic compounds in bioreactors. Water Sci Technol 1996, 33:289-296. 67. Park J-B, Lee S-H, Lee J-W, Lee C-Y: Lab scale experiments for permeable reactive barriers against contaminated groundwater with ammonium and heavy metals using clinoptilolite (01-29B). J Hazard Mater 2002, 95:65-79. 83. Shimomura T, Suda F, Uchiyama H, Yagi O: Biodegradation of trichloroethylene by Methylocystis sp. strain M immobilized in gel beads in a fluidized-bed bioreactor. Water Res 1997, 31:2383-2386. 68. Ake CL, Wiles MC, Huebner HJ, McDonald TJ, Cosgriff D, Richardson MB, Donnelly KC, Phillips TD: Porous organoclay composite for the sorption of polycyclic aromatic hydrocarbons and pentachlorophenol from groundwater. Chemosphere 2003, 51:835-844. The results of this paper suggest that organo-clays should be supported on granular activated carbon and not alumino-silicate structures to increase the efficiency of sorption. This seems intuitive, however as organo-clays may be useful for maintaining microbial populations during bioremediation, there is more work needed on the bioavailability of contaminants sorbed to these types of materials. 84. Hirl PJ, Irvine RL: Reductive dechlorination of perchloroethylene using anaerobic sequencing batch biofilm reactors (AnSBBR). Water Sci Technol 1997, 35:49-56. Current Opinion in Microbiology 2004, 7:227–238 85. Komatsu T, Shinmyo J, Momonoi K: Reductive transformation of tetrachloroethylene to ethylene and ethane by an anaerobic filter. Water Sci Technol 1997, 36:125-132. 86. Daugulis J: Two-phase partitioning bioreactors: a new technology platform for destroying xenobiotics. Trends Biotechnol 2001, 19:457-462. www.sciencedirect.com Engineered passive bioreactive barriers: risk-managing the legacy of industrial soil and groundwater pollution Kalin 235 87. Elmidaoui MA, Tahaikt M, Chay L, Taky M, Elmghari M, Hafsi M: Selective nitrate removal by coupling electrodialysis and a bioreactor. Desalination 2003, 153:389-397. 88. Mansell O, Schroeder ED: Hydrogenotrophic denitrification in a microporous membrane bioreactor. Water Res 2002, 36:4683-4690. 89. Kimura K, Nakamura M, Watanabe Y: Nitrate removal by a combination of elemental sulfur-based denitrification and membrane filtration. Water Res 2002, 36:1758-1766. 90. Min B, Evans PJ, Chu AK, Logan BE: Perchlorate removal in sand and plastic media bioreactors. Water Res 2004, 38:47-60. The bioreactor in this paper was inoculated with a specific strain and relates to previous work done on both mixed and pure cultures. The concept represents a highly engineered approach to biodegradation of contaminants in water. 91. Pardieck L, Bouwer EJ, Stone AT: Hydrogen peroxide use to increase oxidant capacity for in situ bioremediation of contaminated soils and aquifers: a review. J Contam Hydrol 1992, 9:221-242. 92. Truax D, Britto R, Sherrard JH: Bench-scale studies of reactor-based treatment of fuel-contaminated soils. Waste Management 1995, 15:351-357. 93. Wong JWC, Wan CK, Fang M: Pig manure as a co-composting material for biodegradation of PAH-contaminated soil. Environ Technol 2002, 23:15-26. 94. Saner M, Bollier D, Schneider K, Bachofen R: Mass transfer improvement of contaminants and nutrients in soil in a new type of closed soil bioreactor. J Biotechnol 1996, 48:25-35. 95. Zappi ME, Rogers BA, Teeter CL: Bioslurry treatment of a soil contaminated with low concentrations of total petroleum hydrocarbons. J Hazard Mater 1996, 46:1-12. 96. Cassidy DP, Irvine RL: Biological treatment of a soil contaminated with diesel fuel using periodically operated slurry and solid phase reactors. Water Sci Technol 1997, 35:185-192. 97. Glaser JA: Utilization of slurry bioreactors for contaminated solids treatment – an overview. 4th International In Situ and On-Site Bioremediation Symposium, New Orleans 1997, 5:123-130. 98. Truax DD: Bench-scale studies of reactor-based treatment of fuel-contaminated soils. Fuel Energy Abstr 1997, 38:47. 99. Steinle P, Stucki G, Bachofen R, Hanselmann KW: Alkaline soil extraction and subsequent mineralization of 2,6dichlorophenol in a fixed-bed bioreactor. Bioremediation J 1999, 3:223-232. 100. Wang Z: Application of biofilm kinetics to the sulfur/lime packed bed reactor for autotrophic denitrification of groundwater. Water Sci Technol 1998, 37:97-104. 101. Katsoyiannis A, Zouboulis H, Althoff H, Bartel H: As(III) removal from groundwaters using fixed-bed upflow bioreactors. Chemosphere 2002, 47:325-332. 102. Logan BE, LaPoint D: Treatment of perchlorate- and nitratecontaminated groundwater in an autotrophic, gas phase, packed-bed bioreactor. Water Res 2002, 36:3647-3653. 103. Losi ME, Giblin T, Hosangadi V, Frankenberger WT Jr: Bioremediation of perchlorate-contaminated groundwater using a packed bed biological reactor. Bioremediation J 2002, 6:97-103. 104. Nano G, Borroni NA, Rota R: Combined slurry and solid-phase bioremediation of diesel contaminated soils. J Hazard Mater 2003, 100:79-94. This paper shows the optimization required to gain the most efficient engineering approach. What is lacking is a combined understanding of how the processes of microbial biotransformation changed with different parameters. There is a need for joined-up thinking between microbiologists and engineers in this area. 105. Schoefs O, Dochain D, Perrier M, Samson R: Estimation of the hydrodynamic and biokinetic models of soil bioremediation processes. Chem Eng Res Des 2003, 81:1279-1288. www.sciencedirect.com 106. Troquet J, Larroche C, Dussap CG: Evidence for the occurrence of an oxygen limitation during soil bioremediation by solid-state fermentation. Biochem Eng J 2003, 2-3:103-112. This paper presents detailed results of four fixed bed and one rotating bioreactors, in particular there is detailed data on the influence of different operating variables on the biodegradation kinetics presented. This is the type of study where it would interesting to compare changes to microbial populations at the molecular level concurrently. 107. Stembal T, Markic MO, Ribicic N, Briski F, Sipos L: Removal of ammonia, iron and manganese from Groundwaters of northern Croatia–pilot plant studies. Process Biochem 2004, in press. 108. Hess P, Höhener D, Hunkeler D, Zeyer J: Bioremediation of a diesel fuel contaminated aquifer: simulation studies in laboratory aquifer columns. J Contam Hydrol 1996, 23:329-345. 109. Hunkeler D, Jörger D, Häberli K, Höhener P, Zeyer J: Petroleum hydrocarbon mineralization in anaerobic laboratory aquifer columns. J Contam Hydrol 1998, 32:41-61. 110. Kao CM, Chen SC, Su MC: Laboratory column studies for evaluating a barrier system for providing oxygen and substrate for TCE biodegradation. Chemosphere 2001, 44:925-934. 111. Nyman L, Caccavo F Jr, Cunningham AB, Gerlach R: Biogeochemical elimination of chromium (VI) from contaminated water. Bioremediation J 2002, 6:39-55. 112. Rasmussen G, Fremmersvik G, Olsen RA: Treatment of creosotecontaminated groundwater in a peat/sand permeable barrier–a column study. J Hazard Mater 2002, 93:285-306. 113. Kao CM, Chen YL, Chen SC, Yeh TY, Wu WS: Enhanced PCE dechlorination by biobarrier systems under different redox conditions. Water Res 2003, 37:4885-4894. An example of using by-products from other processes (in this case sludge-cake) to provide substrates that enhance reductive dechlorination of perchloroethylene. 114. Wang S, Jaffé PR, Li G, Wang SW, Rabitz HA: Simulating bioremediation of uranium-contaminated aquifers; uncertainty assessment of model parameters. J Contam Hydrol 2003, 64:283-307. 115. Ma X, Novak PJ, Clapp LW, Semmens MJ, Hozalski RM: Evaluation of polyethylene hollow-fiber membranes for hydrogen delivery to support reductive dechlorination in a soil column. Water Res 2003, 37:2905-2918. This application has potential for engineered reactive zones. The results of this research show that approximately 5% of the hydrogen is used for reductive dechlorination and the remainder supporting methanogens. 116. Kao CM, Chen SC, Wang JY, Chen YL, Lee SZ: Remediation of PCE-contaminated aquifer by an in situ two-layer biobarrier: laboratory batch and column studies. Water Res 2003, 37:27-38. 117. Moon HS, Ahn KH, Lee S, Nam K, Kim JY: Use of autotrophic sulfur-oxidizers to remove nitrate from bank filtrate in a permeable reactive barrier system. Environ Pollut 2004, 129:499-507. This is a very recent paper clearly showing how laboratory data can provide engineering design information for permeable reactive barrier implementation. 118. Wang LK, Kurylko L, Hrycyk O: Biological process for groundwater and wastewater treatment. Biotechnol Adv 1996, 14:616. 119. Cox CD, Nivens DE, Ripp S, Wong MM, Palumbo A, Burlage RS, Sayler GS: An intermediate-scale lysimeter facility for subsurface bioremediation research. Bioremediation J 2000, 4:69-79. 120. Hunter WJ: Use of vegetable oil in a pilot-scale denitrifying barrier. J Contam Hydrol 2001, 53:119-131. 121. Guerin TF, Horner S, McGovern T, Davey B: An application of permeable reactive barrier technology to petroleum hydrocarbon contaminated groundwater. Water Res 2002, 36:15-24. 122. Ribeiro de Nardi R, Ribeiro M, Zaiat M, Foresti E: Anaerobic packed-bed reactor for bioremediation of gasolinecontaminated aquifers. Process Biochem 2004, in press. Current Opinion in Microbiology 2004, 7:227–238 236 Ecology and industrial microbiology A chemical engineering paper that validates the application of a technology through laboratory analysis. 123. Environmental Biotechnology: Principles and Applications, Proceedings of the International Symposium on Environmental Biotechnology, held at the University of Waterloo, Ontario, Canada, July 4-8, 1996, Edited by Moo-Young M, Anderson WA, Chakrabarty AM. Kluwer Academic Publishers; ISBN 0-7923-3877-4. 124. Edil TB, Kim JY, Park JK: Reactive barriers for containment of organic compounds. Proc. Int. Symposium 3rd Environ Geotechnol 1996, 1:523-532. 125. Warith M, Fernandes L, Gaudet N: Design of in situ microbial filter for the remediation of naphthalene. Waste Management 1999, 19:9-25. 126. Kao CM, Lei SE: Using a peat biobarrier to remediate PCE/TCE contaminated aquifers. Water Res 2000, 34:835-845. 127. Benner SG, Gould WD, Blowes DW: Microbial populations associated with the generation and treatment of acid mine drainage. Chem Geol 2000, 169:435-448. 128. Kao CM, Chen SC, Liu JK: Development of a biobarrier for the remediation of PCE-contaminated aquifer. Chemosphere 2001, 43:1071-1078. 129. Beeman RE, Bleckmann CA: Sequential anaerobic-aerobic treatment of an aquifer contaminated by halogenated organics: field results. J Contam Hydrol 2002, 57:147-159. 130. McGovern T, Guerin TF, Horner S, Davey B: Design, construction and operation of a funnel and gate in situ permeable reactive barrier for remediation of petroleum hydrocarbons in groundwater. Water Air Soil Pollut 2002, 136:11-31. 131. Benner SG, Blowes DW, Ptacek CJ, Mayer KU: Rates of sulfate reduction and metal sulfide precipitation in a permeable reactive barrier. Appl Geochem 2002, 17:301-320. 132. Ferguson AS, Doherty R, Larkin MJ, Kalin RM, Irvine V, Ofterdinger US: Toxicity assessment of a former manufactured gasplant. Bull Environ Contam Toxicol 2003, 71:21-30. 133. Amos PW, Younger PL: Substrate characterisation for a subsurface reactive barrier to treat colliery spoil leachate. Water Res 2003, 37:108-120. A wonderful field demonstration of a bioreactive permeable reactive barrier system. 134. Schipper LA, Barkle GF, Hadfield JC, Vojvodic-Vukovic M, Burgess CP: Hydraulic constraints on the performance of a groundwater denitrification wall for nitrate removal from shallow groundwater. J Contam Hydrol 2004, 69:263-279. This paper presents field validation of transport and rates of biodegradation of nitrate. 135. Devlin JF, Katic D, Barker JF: In situ sequenced bioremediation of mixed contaminants in groundwater. J Contam Hydrol 2004, 69:233-261. All who are interested in sequential treatment steps during passive bioremediation should read this paper. This is an extensive publication providing the ‘whole’ picture for combined anaerobic/aerobic degradation of mixed chlorinated hydrocarbons and benzene, toluene, ethylbenzene and the xylenes. 136. McGeough KL, Ferguson AS, Walsh KP, Larkin MJ, Ofterdinger US, Kalin RM: Laboratory-based feasibility trials of BTEX biodegradation within a biological permeable reactive barrier. In In Situ and On-Site Bioremediation—2003. Proceedings of the Seventh International In Situ and On-Site Bioremediation Symposium (Orlando, FL; June 2003). Edited by Magar VS, Kelley ME. Batelle Press; 2004. A paper that shows how laboratory experiments are used to develop design parameters for bioreactive barriers. 137. Keck J, Sims RC, Coover M, Park K, Symons B: Evidence for co-oxidation of polynuclear aromatic hydrocarbons in soil. Water Res 1989, 23:1467-1476. 138. Chang BV, Chang SW, Yuan SY: Anaerobic degradation of polycyclic aromatic hydrocarbons in sludge. Advances in Environmental Research 2003, 7:623-628. Current Opinion in Microbiology 2004, 7:227–238 An interesting paper that shows, as expected, that sludge from a petrochemical water treatment plant is more adapted to polycyclic aromatic hydrocarbon (PAH) degradation. However, the relative rates of reactions for the main PAHs were different when compared with municipal sludge. A good candidate for application of molecular techniques. 139. Allen CCR, Boyd DR, Kulakov LA, Larkin MJ, Reid KA, Sharma ND, Wilson K: Metabolism of naphthalene, 1-naphthol, indene and indole in Rhodococcus sp NCIMB12038. Appl Environ Microbiol 1997, 63:151-155. 140. Ramsay JA, Li H, Brown RS, Ramsay BA: Naphthalene and anthracene mineralization linked to oxygen, nitrate, Fe(III) and sulphate reduction in a mixed microbial population. Biodegradation 2003, 14:321-329. 141. Wilson SC, Jones KC: Bioremediation of soil contaminated with polynuclear aromatic hydrocarbons (PAHs): A review. Environ Pollut 1993, 81:229-249. 142. Miller KM, Suidan MT, Sorial GA, Khodadoust AP, Acheson CM, Brenner RC: Anaerobic treatment of soil wash fluids from a wood preserving site. Water Sci Technol 1998, 38:63-72. 143. Koran KM, Suidan MT, Khodadoust AP, Sorial GA, Brenner RC: Effectiveness of an anaerobic granular activated carbon fluidized-bed bioreactor to treat soil wash fluids: a proposed strategy for remediating PCP/PAH contaminated soils. Water Res 2001, 35:2363-2370. 144. Saponaro S, Bonomo L, Petruzzelli G, Romele L, Barbafieri M: Polycyclic aromatic hydrocarbons (PAHs) slurry phase bioremediation of a manufacturing gas plant (MGP). Site Aged Soil. Water Air Soil Pollut 2002, 135:219-236. 145. http://www.prb-net.qub.ac.uk/eerg/dissemination/wpm/ index.htm. 146. Lee S, Cutright T: Bioremediation of polycyclic aromatic hydrocarbon-contaminated soil. J Clean Prod 1995, 3:255. 147. Oesterholt FIHM, Pluim MP, de Vries PW: Groundwater treatment at the former gas work remediation site ‘griftpark’ in Utrecht, the Netherlands. Results of the semi-permanent testing facility. Water Sci Technol 1997, 35:165-172. 148. Doherty R, Ofterdinger US, Yang Y, Dickson K, Kalin RM: Observed and modelled hydraulic aquifer response to slurry wall installation at the former Gasworks Site, Portadown (Northern Ireland, U.K.). In Advanced Groundwater Remediation: Active And Passive Technologies. Edited by Simon FG, Meggyes T, McDonald CM. Thomas Telford Press; 2001:Chapter 15. 149. Guerin TF: A pilot study for the selection of a bioreactor for remediation of groundwater from a coal tar contaminated site. J Hazard Mater 2002, 89:241-252. 150. Ferguson AS, Larkin MJ, Irvine V, McGeough KL, Ofterdinger US, Kalin RM: Characterization of indigenous microorganisms at a former manufactured gas plant. In In Situ and On-Site Bioremediation—2003. Proceedings of the Seventh International In Situ and On-Site Bioremediation Symposium (Orlando, FL; June 2003). Edited by Magar VS, Kelley ME. Batelle Press; 2004. 151. Kalin RM, Doherty R: CIRIA remediation case study: permeable reactive barriers. In Non-Biological Methods For The Assessment And Remediation Of Contaminated Land – Case Studies. Edited by Barr D, Bardos RP, Nathaniel CP. Classic House, London: CIRIA Press ISBN 0 86017 588 X; 2003:113-121. 152. Hund K, Traunspurger W: Ecotox-evaluation strategy for soil bioremediation exemplified for a PAH-contaminated site. Chemosphere 1994, 29:371-390. 153. Gersberg RM, Carroquino MJ, Fischer DE, Dawsey J: Biomonitoring of toxicity reduction during in situ bioremediation of monoaromatic compounds in groundwater. Water Res 1995, 29:545-550. 154. Mandelbaum RT, Shati MR, Ronen D: In situ microcosms in aquifer bioremediation studies. FEMS Microbiol Rev 1997, 20:489-502. 155. Balba MT, Al-Awadhi N, Al-Daher R: Bioremediation of oilcontaminated soil: microbiological methods for feasibility assessment and field evaluation. J Microbiol Methods 1998, 32:155-164. www.sciencedirect.com Engineered passive bioreactive barriers: risk-managing the legacy of industrial soil and groundwater pollution Kalin 237 156. Franzmann PD, Zappia LR, Power TR, Davis GB, Patterson BM: Microbial mineralisation of benzene and characterisation of microbial biomass in soil above hydrocarbon-contaminated groundwater. FEMS Microbiol Ecol 1999, 30:67-76. 157. Baker RJ, Baehr AL, Lahvis MA: Estimation of hydrocarbon biodegradation rates in gasoline-contaminated sediment from measured respiration rates. J Contam Hydrol 2000, 41:175-192. 158. Kao CM, Chen SC, Liu JK, Wang YS: Application of microbial enumeration technique to evaluate the occurrence of natural bioremediation. Water Res 2001, 35:1951-1960. 159. Namocatcat JA, Fang J, Barcelona MJ, Quibuyen ATO, Abrajano TA Jr: Trimethylbenzoic acids as metabolite signatures in the biogeochemical evolution of an aquifer contaminated with jet fuel hydrocarbons. J Contam Hydrol 2003, 67:177-194. 160. Chaineau CH, Yepremian C, Vidalie JF, Ducreux J, Ballerini D: Bioremediation of a crude oil-polluted soil: biodegradation, leaching and toxicity assessments. Water Air Soil Pollut 2003, 144:419-440. 161. Bodour AA, Wang JM, Brusseau ML, Maier RM: Temporal change in culturable phenanthrene degraders in response to long-term exposure to phenanthrene in a soil column system. Environ Microbiol 2003, 5:888-895. 162. Lefaux S, Manceau A, Benguigui L, Campistron I, Laguerre A, Laulier M, Leignel V, Tremblin G: Continuous automated measurement of carbon dioxide produced by microorganisms in aerobic conditions: application to proteic film biodegradation. Comptes Rendus Chimie 2004, in press. This paper focuses on biodegradation of proteic films and presents monitoring that could be used for automated measure of respiration for permeable reactive barriers. Another interesting point is that the research was undertaken in response to impending EU legislation. 163. Hall JA, Kalin RM, Larkin M, Allen C, Harper D: Variation in stable carbon isotope fractionation during aerobic degradation of Phenol and Benzoate by contaminant degrading bacteria. Org Geochem 1998, 30:801-811. 164. Hammer BT, Kelley CA, Coffin RB, Cifuentes LA, Mueller JG: 13C values of polycyclic aromatic hydrocarbons collected from two creosote-contaminated sites. Chem Geol 1998, 152:43-58. 165. Conrad ME, Templeton AS, Daley PF, Alvarez-Cohen L: Isotopic evidence for biological controls on migration of petroleum hydrocarbons. Org Geochem 1999, 8:843-859. 166. Richnow HH, Annweiler E, Koning M, Lüth J-C, Stegmann R, Garms C, Francke W, Michaelis W: Tracing the transformation of labelled 13C phenanthrene in a soil bioreactor. Environ Pollut 2000, 108:91-101. 167. Schroth MH, Kleikemper J, Bolliger C, Bernasconi SM, Zeyer J: In situ assessment of microbial sulfate reduction in a petroleum-contaminated aquifer using push-pull tests and stable sulfur isotope analyses. J Contam Hydrol 2001, 51:179-195. 168. Bailey VL, McGill WB: Fate of 14C-labeled pyrene in a creosote and octadecane in an oil-contaminated soil. Soil Biol Biochem 2004, 34:423-433. A paper that shows results using isotope labels to determine the long-term fate of carbon from contaminant substrates after biodegradative activity. 169. Muyzer G, DeWaal EC, Uilterlinden UAG: Profiling of complex microbial populations by denaturing gradient gel electrophoresis analysis of polymerase chain reactionamplified genes coding for 16srRNA. Appl Environ Microbiol 1993, 59:695-700. 170. Murrell JC, McDonald IR, Bourne DG: Molecular methods for the study of methanotroph ecology. FEMS Microbiol Ecol 1998, 27:103-114. 171. Brigmon RL, Franck MM, Bray JS, Scott DF, Lanclos KD, Fliermans CB: Direct immunofluorescence and enzyme-linked immunosorbent assays for evaluating organic contaminant degrading bacteria. J Microbiol Methods 1998, 32:1-10. 172. Muyzer G, Smalla K: Applications of denaturing gradient gel electrophoresis (DGGE) and temperature gradient gel www.sciencedirect.com electrophoresis (TGGE) in microbial ecology. Antonie Van Leeuwenhoek 1998, 73:127-141. 173. Torsvik V, Daae FL, Sando RA, Øvrea UL: Novel techniques for analysing microbial diversity in natural and perturbed environments. J Biotechnol 1998, 64:53-62. 174. Bundy JG, Paton GI, Campbell CD: Microbial communities in different soil types do not converge after diesel contamination. J Appl Microbiol 2002, 92:276-288. 175. Robertson WJ, Franzmann PD, Mee BJ: Indirect immunofluorescence and FISH for enumerating contaminated site sulfate-reducers. Bioremediation J 2002, 6:25-38. 176. Mills DK, Fitzgerald K, Litchfield CID, Gillevet PM: A comparison of DNA profiling techniques for monitoring nutrient impact on microbial community composition during bioremediation of petroleum-contaminated soils. J Microbiol Methods 2003, 54:57-74. This paper is a good recent example of how molecular techniques can be used to show changes in populations that result from different nutrient additions over time. 177. Mesarch MB, Nakatsu CH, Nies L: Bench-scale and field-scale evaluation of catechol 2,3-dioxygenase specific primers for monitoring BTX bioremediation. Water Res 2004, 38:1281-1288. This is an important new paper which presents both lab and field-scale results for the application of molecular genetic techniques to monitor specific enzyme activity 178. Kosson DS, Agnihotri GC, Ahlert RC: Modeling and simulation of a soil-based microbial treatment process. J Hazard Mater 1987, 14:191-211. 179. Panikov NS: Mechanistic mathematical models of microbial growth in bioreactors and in natural soils: Explanation of complex phenomena. Math Comput Simul 1996, 42:179-186. 180. Nakhla G: Biokinetic modelling of in situ bioremediation of BTX compounds–impact of process variables and scale up implications. Water Res 2003, 37:1296-1307. The design of long-term bioreactive barriers will depend on an understanding of the uncertainty applied to design criteria such as kinetics. This paper provides the reader with an additional parameter — that of variable groundwater velocity. 181. Batstone DJ, Keller J, Blackall LL: The influence of substrate kinetics on the microbial community structure in granular anaerobic biomass. Water Res 2004, 38:1390-1404. The biofilm modeling and molecular results presented in this publication need to be linked to modeling of the full-scale processes seen in other papers. The approach of this work would be very useful for long-term prediction of biofilm stability if it were coupled to modeling of a bioreactive engineered permeable reactive barrier system. 182. Thullner M, Schroth MH, Zeyer J, Kinzelbach W: Modeling of a microbial growth experiment with bioclogging in a two-dimensional saturated porous media flow field. J Contam Hydrol 2004, 70:37-62. This is a very important new paper that has developed a model for longterm microbial biofilm formation within the modeling of fluid flow and contaminant transport within a porous matrix. 183. Gannon JT, Mingelgrin U, Alexander M, Wagenet RJ: Bacterial transport through homogeneous soil. 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