NOV 41994 United States Environmental Protection Agency Robert S. Kerr Environmental Research Laboratory Ada OK 74820 Research and Development EPA/600/SR-94/120 September 1994 EPA Project Summary Evaluation of Technologies for In-Situ Cleanup of DNAPL Contaminated Sites Dennis G. Grubb and Nicolas Sitar Ground-water contamination by nonaqueous phase liquids poses one of the greatest remedial challenges In the field of environmental engineering. Denser-than-water nonaqueous phase liquids (DNAPLs) are especially prob- lematic due to their tow water solubil- ity, high density, and capillary forces arising from Interfaclal tension between the DNAPLs and water. As a result, conventional pump-and-treat tech- nologies have met poor success in remediation of DNAPL-contaminated aquifers. In certain situations, conven- tional pump-and-treat methods may actually extend existing contamination into previously uncontamlnated areas. The problems associated with current pump-and-treat remedial approaches have served as the Impetus to develop alternative technologies to accelerate In-situ DNAPL contamination remedia- tion. This report provides a review and technical evaluation of /n-s/fu technolo- gies for remediation of DNAPL con- tamination occurring below the ground water table. Various In-situ technolo- gies are reviewed and are evaluated on the basis of their theoretical back- ground, field implementation, level of demonstration and performance, waste, technical and site applicability/limita- tions, and cost and availability. This Project Summary was developed by EPA's Robert S. Kerr Environmental Research Laboratory, Ada, OK, to an- nounce key findings of the research project that Is fully documented In a separate report of the same title (see Project Report ordering Information at back). Introduction This report assesses in-situ treatment technologies as they pertain to the treat- ment, mobilization, and recovery of DNAPLs from the subsurface. It identifies in-situ technologies that remediate DNAPLs below the water table; second- ary importance is placed on contaminants dissolved in the aqueous phase. Reme- dial options are controlled by technology evaluation and selection, site consider- ations, regulations, cost, extent of con- tamination, and presence of other waste types. DNAPL Fate and Transport Processes A DNAPL is a sparingly soluble hydro- carbon having a specific gravity greater than that of water at a typical soil tem- perature, usually less than 20°-25°C. The distribution of a DNAPL within the subsur- face results from chemical and physical interactions among the DNAPL, pore wa- ter, pore gases, and porous media. Four phases can be present in the subsurface: the gas phase (in the vadose zone); the solid phase (rock, soil grains, soil organic matter); the aqueous (polar) phase; and the DNAPL (nonpolar phase). For the DNAPL to migrate as a separate phase in any direction, both the capillary pressure resisting DNAPL fbw and the DNAPL re- tention capacity of the soil must be ex- ceeded. The report predicts how hydrophobia compounds will partition in a complex sub- surface environment, and to what extent in-situ technologies will affect partitioning. Two classes of equilibria problems exist: (1) those where only sparingly soluble hy- drocarbons are present, in which the ob- jective is to predict the evolution of the composition of the multicomponent non- aqueous phase liquid pool over time, con- sidering all partitioning that may take place; and (2) those where natural or synthetic surfactants or hydrophilic organic solvents Printed on Recycled Paper ------- such as alcohols, ethers, ketones, amines, nitriles are also present, in which the ob- jective is to predict their influence on the resulting chemical equilibria. Injection, extraction, observation wells, other invasive monitoring, sampling, and remedial structures locally disrupt the stratigraphy and therefore introduce bias. Sampling data can often be misleading relative to the nature and extent of con- tamination, principally in the delineation of DNAPL in the subsurface. Frequently the importance of mutticomponent-multiphase equilibria and interphase transport phe- nomena has been ignored or underesti- mated. Soil heterogeneity affects DNAPL fate and transport. The site stratigraphy af- fects the distribution of the DNAPL in the subsurface, and the contaminant distribu- tion then plays a critical role in the selec- tion of the overall approach for site remediation. Ultimately, the success of any passive or active in-situ technology is largely associated with its susceptibility to soil heterogeneities and its ability to favor- ably alter the DNAPL properties to facili- tate recovery or remediation. Successful technologies also have to be able to adapt to other site-specific con- ditions such as depth to the water table, depth of the contaminated zone, volume of contaminated soil, site access, and man- made structures. Remedial goals often require that a baseline aqueous contaminant concentra- tion be attained or that in excess of 99% of the DNAPL be treated or recovered. This standard poses a challenge to many technologies. Technology Evaluation Several of the evaluated technologies were not originally developed for remedia- tion of contaminated sites, much less DNAPLs. As a result, some of the tech- nologies have not yet been demonstrated on DNAPLs, and, owing to their develop- mental stage, have not been demonstrated in the field below the water table. Some in-situ technologies that have potential ap- plicability to remediation of DNAPLs oc- curring below the water table have been demonstrated in the vadose zone only. However, the evaluation of technologies used to clean up contamination in the vadose zone is not included in this report. Also, several in-situ technologies have been fully demonstrated only in non-envi- ronmental applications and are currently being adapted for environmental applica- tions. In all cases, the applicability to re- mediation of DNAPLs occurring below the water table is nonetheless considered. Biological Processes In-situ biodegradation is a process in which aqueous phase organic compounds are completely or partially metabolized by microorganisms situated in the subsurface. Bacteria are largely responsible for the biological transformations that occur in porous media and are generally consid- ered as a stationary phase either through attachment to solid surfaces or via ag- glomeration. These organisms convert natural and xenobiotic organic compounds into energy and end products and use a portion of the organic material for cell syn- thesis. Metabolic processes of aerobic and anaerobic microbial consortia are distin- guished by the nature of carbon substrate use, and three metabolic processes are recognized: primary metabolism, second- ary metabolism, and cometabolism. The metabolic use of a compound depends on its molecular structure, concentration, en- vironmental conditions, bioavailability of nutrients, presence of competing or inhibi- tory substrates, the nature of the micro- bial consortia and the enzymes and cofactors they possess, and toxicity ef- fects. Primary metabolism of an organic com- pound occurs when it yields sufficient energy for cell main- tenance and growth and is present at concentrations large enough to sustain the microbial population. Petroleum hydrocarbons are good ex- amples of primary substrates, while com- pounds such as ammonia can serve as a primary energy source but not a carbon source. Many stoichiometric relationships describing the oxidation and reduction of organic compounds by microbes are known. From the stoichiometric relations, nutrient demands can be estimated and Monod kinetics can be used to relate the growth and decay of the microbial consor- tia to the degradation reactions. Secondary metabolism describes the use of trace organic compounds that cannot sustain microbial growth. Cometabolism occurs when nonspecific microbial enzymes or cofactors biotrans- form organic compounds that provide insignificant energy and organic carbon for growth. Cometabolism is one of the major mechanisms in the transformation of chlorinated hydrocarbons and pesti- cides. Electrolytic Processes t In-situ electrolytic processes use applied electric fields to enhance organic contami- nant removal. The effectiveness of these processes in soils is controlled by coupled flow phenomena. Usually the flow results from the presence of fluid, heat, electrical, and chemical flow potentials; any of these potentials may be created even though only one driving force is applied. Containment and Ground Modification Containment systems and ground modi- fication methods are used to contain and immobilize dissolved contaminants and, in certain cases, DNAPLs. Containment systems are usually placed on the periph- ery of the contaminated area so that the encompassed area becomes isolated from its surroundings. Impermeable barriers and ground-water injection/extraction systems are examples of containment systems. The ground modification methods are usually confined to DNAPL source areas and im- mobilize or neutralize the contaminants. Stabilization/solidification (S/S), vitrification, and permeable treatment walls are ex- amples of ground modification. Contain- ment and ground modification can be either passive or active; the distinction is madi on the required energy expenditure afte. installation. Immobilization of contaminants is achieved by neutralization, precipitation, sorption, and physical encapsulation of the contaminants within a solidified soil matrix. The major issues surrounding in- situ S/S are chemical compatibility and the durability and teachability of the treated soil mass. In-situ permeable treatment walls are granular backfill walls that provide treat- ment of dissolved contaminants but no containment or immobilization. The com- position of the porous backfill can pro- mote favorable conditions for in-situ biodegradation, precipitation, and chemi- cal oxidation or reduction. The major is- sues regarding in-situ permeable treatment walls pertain to changes in ground-water flow direction, clogging, long-term perfor- mance, and incomplete treatment of wastes. Soil Washing Processes In-situ soil washing (or fluid flushing/ flooding) relies on fluid-fluid displacement processes to enhance contaminant re- moval. Fluids can be injected into the po- rous media to mobilize the resident pore fluids, water, and DNAPL. This is done b) a combination of physical forces that can ------- be aided by favorably altering chemical partitioning so that bulk fluid properties change. The exact nature of the displace- ment and the prevailing physical and chemical behavior occurring in these sys- tems depends on the liquid properties and environmental conditions. Air Stripping Processes In-situ air stripping processes rely on the air circulation through the subsurface to remove volatile DNAPLs from the sub- surface. The applications considered here, in-situ air sparging, vacuum extraction, and vacuum vaporizer wells, differ from con- ventional air stripping and soil vapor ex- traction in the vadose zone in that they operate in both the saturated and unsat- urated zones. Air sparging and vacuum extraction en- tail the injection of clean air directly into the saturated zone. Stripping occurs in the porous medium, and volatilized con- taminants are recovered by vapor extrac- tion wells nested in the vadose zone. Vacuum vaporizer wells, or UVBs, create water recirculation cells in the porous me- dia. Stripping is performed "in-well," and contaminant-laden vapors are collected at the top of the well. Water is recycled back into the aquifer. UVBs can also simulta- neously recover soil vapors from the va- dose zone. Both processes apply to the recovery of volatile and semi-volatile DNAPLs only. Sparging may also result in uncontrolled migration of DNAPL out of the treatment zone. Enhanced biostimulation may be a beneficial byproduct of both processes. Both technologies are commercially avail- able and used. Thermal Processes Thermal and thermally enhanced pro- cesses deliver thermal energy into the sub- surface: the CROW® process uses hot water and/or low qualify steam injection; in-situ steam enhanced extraction (SEE) relies on high quality steam injection; and radio frequency heating and in-situ vitrifi- cation (ISV) facilitate heating using micro- wave and electrical arrays, respectively. During these processes, steam and hot water progress through cool porous me- dia and heat the interstitial fluids and po- rous media. These fluid-fluid displacement processes are analogous to liquid-liquid displacement processes with the added complexity of heat transfer. The contami- nants can be recovered as vaporized gases and as dissolved- and separate- phase liquids. The effectiveness of the CROW® pro- cess and SEE is controlled by the thermo- dynamics and hydrodynamics of hot wa- ter and steam displacement in porous media. Thus, the thermal properties of both the porous media and the pore fluids become important. The orientation and shape of the propagating steam fronts are governed by the matrix heterogeneities, geometry of the aquifer, initial moisture and boundary conditions, steam quality, injection rates, and the ratio of buoyancy to viscous forces. In saturated homoge- neous isotropic porous media, the ratio of buoyancy to viscous forces is important in terms of gravity override and effective sweep-out. The same principles hold for condensation fronts propagating through layered media, but the temperature pro- files and fronts will be curved at layer interfaces owing to intrinsic permeability differences. When gravity effects are neg- ligible, the behavior of propagating fronts can be predicted and controlled. Radio frequency heating achieves sub- surface heating by using an electrode ar- ray system to transmit electromagnetic waves through the porous media. In-situ moisture is converted to a steam front that propagates through porous media thus displacing other pore fluids, including DNAPLs. ISV also employs an electrode array system but for the purposes of current flow. Large current flows cause electrical resistance (joule) heating of the soil to the melting point. During this process, DNAPLs can be volatilized and pyrolized. The CROW®, SEE, and radio frequency heating processes have their origins in the enhanced oil recovery business. ISV was developed for the S/S of wastes con- taining radionuclides. All of these tech- nologies have been demonstrated at the pilot scale, but only CROW® and SEE have been successfully demonstrated in the saturated zone. A full-scale demon- stration of SEE is in progress. Results and Discussion This study was conducted between De- cember 1991 and May 1993. No actual experiments were conducted. Approxi- mately 400 references were compiled dur- ing this study. Information was collected from journal articles, conference proceed- ings, vendor and manufacturer fact sheets and literature, and federal, state, and lo- cal agency reports and publications. The authors also attended a number of confer- ences to obtain information that was as current as possible. To supplement these sources of infor- mation, an "In-situ DNAPL Remediation Technology Description Questionnaire" was developed in cooperation with EPA personnel at the Robert S. Kerr Environ- mental Research Laboratory. The ques- tionnaire was sent to professionals working in the area of DNAPL cleanup. These questionnaires were first mailed in Febru- ary 1992. Positive responses were fol- lowed up with letters and personal contacts. As the project progressed, the correspondence was expanded. Descriptions of the relevant in-situ tech- nologies were then prepared. The follow- ing aspects of each relevant in-situ technology were evaluated: theoretical background, field implementation, level of demonstration and performance, applica- bility/limitations, and cost and availability. Several technologies have been demon- strated. Limitations of the Report The technology descriptions included in the report cannot be considered exhaus- tive because of the following limitations: • short time—18 months poor literature reporting gaps due to unavailability of infor- mation nature of proprietary research and/ or confidential information • stage of development of technol- ogy Therefore, the expected performance of these technologies can be difficult to in- terpret in the context of DNAPL cleanup. While this report can help identify po- tentially applicable in-situ technologies for cleanup of DNAPL-contaminated sites, it should not be the sole basis for selecting a technology for a particular DNAPL at a given site. The report is not a substitute for engineering judgement, analysis, and design. Potential in-situ technologies must be further evaluated by contacting tech- nology developers and by performing bench- and/or pilot-scale treatability tests as necessary under site-specific condi- tions. This is especially true for undemonstrated technologies and for tech- nologies whose success depends heavily on the characteristics of the waste matrix. Conclusions The remediation of DNAPLs faces chal- lenges posed by the site stratigraphy and heterogeneity, the distribution of the con- tamination, and the physical and chemical properties of the DNAPL. A successful technology has to be able to overcome the problems posed by the site complexity and be able to modify the properties of the DNAPL to facilitate recovery, immobi- lization, or degradation. In addition, the ------- methodology must be adaptable to differ- ent site conditions and must be able to meet the regulatory goals. Thermally based technologies are among the most promising. Among ther- mal technologies, SEE is probably the most promising candidate, the CROW® process relies on similar mechanisms; however, it is not dear whether the injec- tion of hot water and low quality steam offers an advantage over SEE. Radio fre- quency heating, which relies on in-situ steam generation to be most effective, has only been tested in the vadose zone. The next group of promising technolo- gies are the soil washing technologies be- cause they can manipulate chemical equilibria and reduce capillary forces. A blend of alkalis, cosolvents, and surfac- tants is probably the best combination for a soil washing application, and each is important for its own reasons; alkalis can saponify certain DNAPLs and affect wet- tability and sorption, cosolvents pro- vide viscous stability and enhance solubility and mass transfer between the aqueous phase and the DNAPL, and surfactants have the largest impacts on solubility and interfacial tension reduction. Water flood- ing is best applied in highly contaminated areas as a precursor to these methods. The thermal and soil washing technolo- gies are best suited for areas that are highly contaminated with DNAPLs. How- ever, these techniques by themselves still may not be able to achieve the currently mandated regulatory cleanup standards. Thus, consideration should be given to' using these technologies in combination with the technologies suitable for long- term plume management. The bioreme- diation techniques and permeable treatment walls hold the best promise. A special problem is posed by mixed wastes, heavy metals and radionuclides mixed with DNAPLs since recovery at the ground surface may not be desirable in many instances. In such instances, S/S and vitrification are the most viable in-situ technologies. Excluding radionuclides, in- situ S/S is the most promising candidate because of its broadly demonstrated ef- fectiveness, cost, and applicability to the saturated zone. Dennis G. Grubb and Nicolas Sitar are with the Department of Civil Engineering, University of California, Berkeley, CA 94720. Stephen G. Schmelllng is the EPA Project Officer (see below). The complete report, entitled "Evaluation of Technologies for In-Situ Cleanup of DNAPL Contaminated Sites," (Order No. PB94-195039; Cost: $27.00; subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield, VA 22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Robert S. Kerr Environmental Research Laboratory U.S. Environmental Protection Agency Ada, OK 74820 United States Environmental Protection Agency Center for Environmental Research Information Cincinnati, OH 45268 Official Business Penalty for Private Use $300 BULK RATE POSTAGE & FEES PAID EPA PERMIT No. G-35 EPA/600/SR-94/120 ------- |