For sites contaminated with chloroethene non-aqueousphase liquids, designing a remediation system that couples in situ chemical oxidation (ISCO) with potassium permanganate (KMnO4) and microbial dechlorination may be complicated because of the potentially adverse effects of ISCO on anaerobic bioremediation processes. Therefore, one-dimensional column studies were conducted to understand the effect of permanganate oxidation on tetrachloroethene (PCE) dechlorination by the anaerobic mixed culture KB-1. Following the confirmation of PCE dechlorination, KMnO4 was applied to all columns at a range of concentrations and application velocities to simulate varied distances from oxidant injection. Immediately following oxidation, reductive dechlorination was inhibited; however, after passing several pore volumes of sterile growth medium through the columns after oxidation, a rebound of PCE dechlorination activity was observed in every inoculated column without the need to reinoculate. The volume of medium required for a rebound of dechlorination activity differed from 1.1 to 8.1 pore volumes (at a groundwater velocity of 4 cm/d), depending on the specific condition of oxidant application.

The presence of coal tars in the subsurface associated with former manufactured gas plants (MGPs) offers a remediation challenge due to their complex chemical composition, dissolution behaviour and recalcitrant characteristics. A former MGP site in Clearwater Beach, Florida was characterized and bench-scale analyses were conducted to assess the potential for in situ chemical oxidation (ISCO) using persulfate to treat MGP residuals. Completion of a conceptual site model identified a homogeneous, silty sand aquifer, with an average hydraulic conductivity of approximately 2.3x10-3 cm/s and a groundwater flow rate of 2 cm/day in the direction of S20°E. Six source zones, three near the water table and three in the deep aquifer were estimated to have a total volume of 108 m3. A multi-level well transect was installed to monitor concentrations of dissolved compounds and to estimate mass discharge downgradient of the source zones over time. On average, the morphology of the aqueous concentrations remained consistent with time. A total mass discharge across the transect of 94 mg/day was estimated for site-specific compounds. Bench-scale tests were conducted on aquifer sediments and groundwater samples. The aquifer was determined to have a low buffering capacity, low chemical oxygen demand, and low natural oxidant interaction (NOI) with persulfate. Aqueous batch experiments identified the potential for iron (II) activated persulfate to reduce concentrations of BTEX and PAHs below method detection limits (MDLs). Unactivated persulfate was able to reduce BTEX concentrations to below MDLs after 14 days; however, the concentration of PAH compounds remained above MDLs after 14 days. Higher iron doses within the system were shown to be more effective in reducing BTEX and PAH compounds. Column experiments designed to mimic site conditions were used to evaluate the feasibility of persulfate treatment on impacted sediments from the Clearwater site. Two sets of column experiments were conducted: one using unactivated persulfate followed by alkaline activated persulfate; and one using iron (II) activated persulfate. On average, unactivated persulfate was able to reduce BTEX and PAH aqueous effluent concentrations by > 75% and 40%, respectively, after a total dose of 60 g/g soil. Two additional doses of alkaline activated persulfate (total persulfate dose of ~80g/g soil) in these columns were able to further reduce effluent BTEX and PAH concentrations by > 90% and > 75%, respectively. Iron (II) activated persulfate reduced effluent BTEX concentrations by > 70% and PAHs by > 65% after a total dose of 35 g/g soil. Average reductions in mass for BTEX and PAH compounds were approximately of 48% and 26% respectively in the iron (II) activated persulfate columns, and 24% and 10%, respectively in the alkaline activated persulfate columns. The potential for the ability to use in situ chemical oxidation using persulfate for the remediation of MGP residuals in the subsurface is evaluated using field measurements and bench-scale experimentation. The reductions observed in aqueous phase compounds in MGP groundwater as observed in the laboratory indicate the potential for reductions in groundwater concentrations at this and other contaminated former MGP sites. However, column experiments, indicating the inability for activated persulfate to reduce all identified compounds in the MGP NAPL suggest source treatment with activated persulfate would not reduce concentrations to below Florida Department of Environmental Protection natural attenuation concentrations.

The purpose of this study was to use controlled release technology combining with in situ chemical oxidation (ISCO) and permeable reactive barrier (PRB) to remediate TCE-contaminated groundwater. In this study, potassium permanganate (KMnO4) releasing material was designed for potassium permanganate release in groundwater. The components of potassium permanganate releasing material included poly (£`-caprolactone) (PCL), potassium permanganate, and starch with a weight ratio of 2:1:0.5. Approximately 63.8% (w/w) of potassium permanganate was released from the material after 76 days of operation. The released was able to oxidize contaminant in groundwater. Results from the solid oxidation demand (SOD) experiment show that the consumption rate increased with increased contaminant concentration. TCE removal efficiency increased with the increased TCE concentration. The second-order rate law can be used to simulate the TCE degradation trend. In the column experiment, results show that the released MnO4- could oxidize TCE and TCE degradation byproducts when 95.6 pore volume (PV) of contaminated groundwater was treated. More than 95% of TCE removal can be observed in the column study. Although the concentration of manganese dioxide (MnO2) began to rise after 8.8 PV of operation, TCE removal was not affected. Results also show that low level of hexavalent chromium was detected (< 0.05 mg/L). Results from the scanning electron microscope (SEM) and energy-dispersive spectroscope (EDX) analyses show that the amounts of manganese and potassium in the materials decreased after the releasing experiment. Results indicate that the concentration of TCE and SOD need to be analyzed before the releasing materials are applied in situ. In the practical application, the releasing materials will not become solid wastes because they are decomposed after use. If this slow-releasing technology can be combined with a permeable reactive barrier system, this technology will become a more economic and environmentally-friendly green remedial system.

Soil and groundwater at many existing and former industrial areas and disposal sites is contaminated by organic solvent compounds that were released into the environment. Organic solvent compounds are heavier than water. When they are released into the subsurface, they tend to adsorb onto the soils and cause the appearance of LNAPL (light nonaqueous phase liquid) and DNAPL (dense nonaqueous phase liquid) pool. The industrial petroleum hydrocarbons (e.g., methyl tertiary-butyl ether, MTBE and benzene) and chlorinated solvent (e.g., trichloroethylene, TCE) are among the most ubiquitous organic compounds found in subsurface contaminated environment. One cost-effective approach for the remediation of the chlorinated solvent and petroleum products contaminated aquifers is the installation of permeable reactive zones or barriers within aquifers. As contaminated groundwater moves through the emplaced reactive zones, the contaminants are removed, and uncontaminated groundwater emerges from the downgradient side of the reactive zones. The objectives of this study were developed to evaluate the feasibility of applying in-situ chemical oxidation (ISCO) barrier and in-situ slow polycolloid-releasing substrate (SPRS) biobarrier system on the control of petroleum hydrocarbons and chlorinated solvent plume in aquifer. In the ISCO barrier system, it contained oxidant-releasing materials, to release oxidants (e.g., persulfate) contacting with water for oxidating contaminants existed in groundwater. In this study, laboratory-scale fill-and-draw experiments were conducted to determine the compositions ratios of the oxidant-releasing materials and evaluate the persulfate release rates. Results indicate that the average persulfate-releasing rate of 7.26 mg S2O82-/d/g was obtained when the mass ratio of sodium persulfate/cement/sand/water was 1/1.4/0.24/0.7. The column study was conducted to evaluate the efficiency of in situ application of the developed ISCO barrier system on MTBE and benzene oxidation. Results from the column study indicate that approximately 86-92% of MTBE and 95-99% of benzene could be removed during the early persulfate-releasing stage (before 48 pore volumes of groundwater pumping). The removal efficiencies for MTBE and benzene dropped to approximately 40-56% and 85-93%, respectively, during the latter part of the releasing period due to the decreased persulfate-releasing rate. Results reveal that acetone, byproduct of MTBE, was observed and then further oxidized completely. Results suggest that the addition of ferrous ion would activate the persulfate oxidation. However, excess ferrous ion would compete with organic contaminants for persulfate, causing the decrease in contaminant oxidation rates. In the SPRS biobarrier system, the food preparation industry has tremendous experiences in producing stable oil-in-water (W/O, 50/50) emulsions with a uniformly small droplet size. Surfactant mixture (71 mg/L of SL and 72 /L of SG) blending with water could yield a stable and the optimal emulsion was considered the best. The small absolute value of the emulsion zeta potential reduces inter-particle repulsion, causing the emulsion droplets to stick to each other when they collided. Overtime, large masses of flocculated droplets can form which then clog the sediment pores. The results can be used to predict abiotic interactions and distribution of contaminant mass expected after SPRS injection, and thus provides a more accurate estimate of the mass of TCE removed due to enhanced biodegradation. The effect of TCE partitioning to the vegetable oil on contaminant migration rates can be approximated using a retardation factor approach, where 0.28 years through a 3 m barrier. In anaerobic microcosm experiments, result show that SPRS can be fermented to hydrogen and acetate could be used as a substrate to simulate reductive dehalorination. The apparent complete removal of nitrate and sulfate by SPRS addition was likely a major factor that promoted the complete reduction of TCE at later stages of this study. Results from the column experiment indicate that occurrence of anaerobic reductive dechlorination in the biobarrier system can be verified by: (1) the oil: water partition coefficients of dissolved TCE into vegetable oil were be used to predict abiotic interactions and distribution of contaminant mass expected after SPRS injection. (2) The SPRS can ferment to hydrogen and acetate could be used as a substrate to simulate reductive dechlorination. The proposed treatment scheme would be expected to provide a more cost-effective alternative to remediate other petroleum hydrocarbons and chlorinated solvents-contaminated aquifers. Experiments and operational parameters obtained from this study provide an example to design a passive barriers system for in-site remediation.

The presence of coal tars in the subsurface associated with former manufactured gas plants (MGPs) offers a remediation challenge due to their complex chemical composition, dissolution behaviour and recalcitrant characteristics. A former MGP site in Clearwater Beach, Florida was characterized and bench-scale analyses were conducted to assess the potential for in situ chemical oxidation (ISCO) using persulfate to treat MGP residuals. Completion of a conceptual site model identified a homogeneous, silty sand aquifer, with an average hydraulic conductivity of approximately 2.3x10-3 cm/s and a groundwater flow rate of 2 cm/day in the direction of S20°E. Six source zones, three near the water table and three in the deep aquifer were estimated to have a total volume of 108 m3. A multi-level well transect was installed to monitor concentrations of dissolved compounds and to estimate mass discharge downgradient of the source zones over time. On average, the morphology of the aqueous concentrations remained consistent with time. A total mass discharge across the transect of 94 mg/day was estimated for site-specific compounds. Bench-scale tests were conducted on aquifer sediments and groundwater samples. The aquifer was determined to have a low buffering capacity, low chemical oxygen demand, and low natural oxidant interaction (NOI) with persulfate. Aqueous batch experiments identified the potential for iron (II) activated persulfate to reduce concentrations of BTEX and PAHs below method detection limits (MDLs). Unactivated persulfate was able to reduce BTEX concentrations to below MDLs after 14 days; however, the concentration of PAH compounds remained above MDLs after 14 days. Higher iron doses within the system were shown to be more effective in reducing BTEX and PAH compounds. Column experiments designed to mimic site conditions were used to evaluate the feasibility of persulfate treatment on impacted sediments from the Clearwater site. Two sets of column experiments were conducted: one using unactivated persulfate followed by alkaline activated persulfate; and one using iron (II) activated persulfate. On average, unactivated persulfate was able to reduce BTEX and PAH aqueous effluent concentrations by > 75% and 40%, respectively, after a total dose of 60 g/g soil. Two additional doses of alkaline activated persulfate (total persulfate dose of ~80g/g soil) in these columns were able to further reduce effluent BTEX and PAH concentrations by > 90% and > 75%, respectively. Iron (II) activated persulfate reduced effluent BTEX concentrations by > 70% and PAHs by > 65% after a total dose of 35 g/g soil. Average reductions in mass for BTEX and PAH compounds were approximately of 48% and 26% respectively in the iron (II) activated persulfate columns, and 24% and 10%, respectively in the alkaline activated persulfate columns. The potential for the ability to use in situ chemical oxidation using persulfate for the remediation of MGP residuals in the subsurface is evaluated using field measurements and bench-scale experimentation. The reductions observed in aqueous phase compounds in MGP groundwater as observed in the laboratory indicate the potential for reductions in groundwater concentrations at this and other contaminated former MGP sites. However, column experiments, indicating the inability for activated persulfate to reduce all identified compounds in the MGP NAPL suggest source treatment with activated persulfate would not reduce concentrations to below Florida Department of Environmental Protection natural attenuation concentrations.

Grande parte das áreas contaminadas conhecidas atualmente advém de práticas passadas onde os cuidados com a proteção à saúde humana e ao meio ambiente eram desconhecidos ou ignorados. O uso indiscriminado de produtos solventes clorados fez com que tais compostos se tornassem uma das principais fontes de contaminação no setor industrial. Por serem compostos de alta toxicidade, quando presentes na água subterrânea, mesmo em baixas concentrações, a tornam imprópria para o consumo. Técnicas de remediação como atenuação natural, ou que envolvam bombeamento e tratamento de água subterrânea contaminada por solventes clorados, vêm sendo substituídas por metodologias químicas destrutivas, por apresentarem resultados satisfatórios em um período de tempo inferior às técnicas utilizadas anteriormente. Este trabalho objetiva apresentar os resultados obtidos em duas áreas industriais onde foram aplicadas técnicas de remediação, envolvendo a redução química in situ, através da injeção de polisulfeto de cálcio e a oxidação química in situ, com a injeção de permanganato de potássio. Em ambas as áreas, os contaminantes organoclorados são os principais compostos de interesse presentes na água subterrânea. A redução química in situ é uma metodologia que utiliza um agente químico para reduzir óxidos de ferro III, presentes naturalmente no aquífero sedimentar, e transformá-los em ferro II que, por sua vez reduzirá contaminantes organoclorados. A principal característica desta metodologia é a eliminação contígua de dois átomos de cloro das moléculas dos contaminantes, o que tende e diminuir ou eliminar o acúmulo de subprodutos tóxicos como cloreto de vinila. Na oxidação química in situ, o agente promove a transferência de elétrons, onde os íons Cl- das moléculas dos contaminantes são substituídos por H+. Devido à baixa reatividade entre o permanganato de potássio e a matriz do aquífero durante as reações de oxidação química, este oxidante pode ser transportado pelos processos advectivo e dispersivo juntamente com o fluxo da água subterrânea e persistir por um período maior de tempo, reagindo com os contaminantes orgânicos. Ensaios de bancada com solo saturado contaminado de uma das áreas de estudo mostraram excelentes resultados na utilização do polisulfeto de cálcio, mas o mesmo não foi observado no teste piloto realizado em campo. Embora tenha sido observada dispersão do produto nas proximidades de pelo menos um dos pontos onde a solução foi injetada, notou-se que não houve redução significativa dos contaminantes, evidenciando que o ferro II não foi eficaz no processo de degradação. Isto pode ter sido ocasionado por uma série fatores, como possíveis reações, características hidráulicas, ou geológicas do meio. Portanto, o prosseguimento desta metodologia como alternativa de remediação para toda a área impactada foi descontinuado, tornando necessário novos estudos para avaliar a melhor técnica aplicável na área. Quanto à área onde foi aplicada a oxidação química, a remediação foi considerada eficiente. Ao longo do período de vinte e dois meses, quando foram realizadas atividades de monitoramento da água subterrânea, observou-se a presença do permanganato de potássio nas áreas mais impactadas das plumas de contaminação, fato que permitiu o processo de transferência de elétrons e consequentemente a oxidação dos contaminantes. Vinte e dois meses após as atividades de injeção, o principal contaminante identificado na área, o 1,-1-dicloroeteno, foi detectado em apenas um ponto com concentração superior a meta de remediação obtida anteriormente à injeção. Considerando que durante a sequência das atividades relacionadas à remediação, este contaminante sofreu alterações em seus valores toxicológicos estabelecidos pela Agência de Proteção Ambiental dos Estados Unidos, e passou a ser considerado um composto não carcinogênico, todos os poços apresentaram-se com concentrações inferiores a nova meta de remediação calculada. Como efeito colateral, foi observado o aumento das concentrações de metais dissolvidos, como: alumínio, bário, cromo e ferro. Tal mobilização de metais para a água subterrânea pode ser considerada temporária. Após o total consumo do permanganato de potássio pelos contaminantes ainda presentes no meio, as características físico-químicas do aquífero retornarão à situação identificada naturalmente, permitindo a precipitação dos metais. / Most of the currently known contaminated areas are the result of past practices, where precautions regarding protection of human health and the environment were either unknown or ignored. The indiscriminate use of chlorinated solvents is the driving factor that has led to such compounds becoming one of the main sources of contamination in the industrial sector. Chlorinated solvents are highly toxic and, when present at even low concentrations in groundwater, they make this resource unfit for human consumption. Such remediation techniques as natural attenuation, or that involve pumping and treatment of groundwater contaminated by chlorinated solvents, are currently being replaced by destructive chemical methods, as they show satisfactory results in a shorter period of time than previously used techniques. This study has the objective of showing the results obtained at two industrial sites where remediation techniques have been used involving in-situ chemical reduction, through injection of calcium polysulfide, and in-situ chemical oxidation, with injection of potassium permanganate. At both sites, organochlorine contaminants are the main compounds of concern present in groundwater. In-situ chemical reduction is a methodology that uses a chemical agent in order to reduce iron III oxides, naturally present in the sedimentary aquifer, and transform them into iron II which, in turn, reduces the organochlorine contaminants. The principal characteristic of this methodology is that of contiguous elimination of two chlorine atoms from contaminant molecules, which tends to reduce or eliminate accumulation of such toxic byproducts as vinyl chloride. In in-situ chemical oxidation, the chemical agent brings about a transfer of electrons, where the Cl- ions of contaminant molecules are replaced by H+ ions. Due to the low degree of reactivity between potassium permanganate and the aquifer matrix during chemical oxidation reactions, this oxidizing agent can be transported via groundwater flow, by advective and dispersive processes, and persist for a longer period of time, reacting with organic contaminants. Bench tests performed with contaminated saturated soil from one of the sites under study showed excellent results through the use of calcium polysulfide; however, the same results were not observed during a pilot test performed in the field. Although product dispersion was observed in the vicinity of at least one of the points where the solution had been injected, it was found that there was no significant reduction of contaminants, showing that iron II was not effective in enhancing the degradation process. This could have been the result of a series of factors, for example, possible reactions or the hydraulic or geological characteristics of the medium. Therefore, it was decided not to continue with use of this methodology as a remediation alternative for the whole impacted area, making it necessary for further studies in order to assess the best technique applicable at the site. With respect to the site where a chemical oxidation approach was adopted, remediation was considered to be effective. Over a period of twenty-two months, during which groundwater monitoring activities were performed, the presence of potassium permanganate was observed in the most impacted areas of the contamination plumes, a fact that allowed for the electron transfer process and, consequently, contaminant oxidation. Twenty-two months after initiation of injection activities, the main contaminant identified at the site (1,1-dichloroethene) was only detected at one point at a concentration exceeding the post-remediation target value established prior to commencing these activities. Considering that, during the sequence of activities related to the remediation process, this contaminant underwent changes in its toxicological values established by the United States Environmental Protection Agency, and came to be considered a non-carcinogenic compound, all wells showed concentrations below the new calculated post-remediation target. As a collateral effect, there was found to be an increase in concentrations of such dissolved metals as aluminum, barium, chromium and iron. Such mobilization of metals to groundwater can be considered a temporary effect. Following complete consumption of potassium permanganate by contaminants still present in the medium, the physical-chemical characteristics of the aquifer will return to the situation occurring naturally, allowing for the precipitation of these metals.

Grande parte das áreas contaminadas conhecidas atualmente advém de práticas passadas onde os cuidados com a proteção à saúde humana e ao meio ambiente eram desconhecidos ou ignorados. O uso indiscriminado de produtos solventes clorados fez com que tais compostos se tornassem uma das principais fontes de contaminação no setor industrial. Por serem compostos de alta toxicidade, quando presentes na água subterrânea, mesmo em baixas concentrações, a tornam imprópria para o consumo. Técnicas de remediação como atenuação natural, ou que envolvam bombeamento e tratamento de água subterrânea contaminada por solventes clorados, vêm sendo substituídas por metodologias químicas destrutivas, por apresentarem resultados satisfatórios em um período de tempo inferior às técnicas utilizadas anteriormente. Este trabalho objetiva apresentar os resultados obtidos em duas áreas industriais onde foram aplicadas técnicas de remediação, envolvendo a redução química in situ, através da injeção de polisulfeto de cálcio e a oxidação química in situ, com a injeção de permanganato de potássio. Em ambas as áreas, os contaminantes organoclorados são os principais compostos de interesse presentes na água subterrânea. A redução química in situ é uma metodologia que utiliza um agente químico para reduzir óxidos de ferro III, presentes naturalmente no aquífero sedimentar, e transformá-los em ferro II que, por sua vez reduzirá contaminantes organoclorados. A principal característica desta metodologia é a eliminação contígua de dois átomos de cloro das moléculas dos contaminantes, o que tende e diminuir ou eliminar o acúmulo de subprodutos tóxicos como cloreto de vinila. Na oxidação química in situ, o agente promove a transferência de elétrons, onde os íons Cl- das moléculas dos contaminantes são substituídos por H+. Devido à baixa reatividade entre o permanganato de potássio e a matriz do aquífero durante as reações de oxidação química, este oxidante pode ser transportado pelos processos advectivo e dispersivo juntamente com o fluxo da água subterrânea e persistir por um período maior de tempo, reagindo com os contaminantes orgânicos. Ensaios de bancada com solo saturado contaminado de uma das áreas de estudo mostraram excelentes resultados na utilização do polisulfeto de cálcio, mas o mesmo não foi observado no teste piloto realizado em campo. Embora tenha sido observada dispersão do produto nas proximidades de pelo menos um dos pontos onde a solução foi injetada, notou-se que não houve redução significativa dos contaminantes, evidenciando que o ferro II não foi eficaz no processo de degradação. Isto pode ter sido ocasionado por uma série fatores, como possíveis reações, características hidráulicas, ou geológicas do meio. Portanto, o prosseguimento desta metodologia como alternativa de remediação para toda a área impactada foi descontinuado, tornando necessário novos estudos para avaliar a melhor técnica aplicável na área. Quanto à área onde foi aplicada a oxidação química, a remediação foi considerada eficiente. Ao longo do período de vinte e dois meses, quando foram realizadas atividades de monitoramento da água subterrânea, observou-se a presença do permanganato de potássio nas áreas mais impactadas das plumas de contaminação, fato que permitiu o processo de transferência de elétrons e consequentemente a oxidação dos contaminantes. Vinte e dois meses após as atividades de injeção, o principal contaminante identificado na área, o 1,-1-dicloroeteno, foi detectado em apenas um ponto com concentração superior a meta de remediação obtida anteriormente à injeção. Considerando que durante a sequência das atividades relacionadas à remediação, este contaminante sofreu alterações em seus valores toxicológicos estabelecidos pela Agência de Proteção Ambiental dos Estados Unidos, e passou a ser considerado um composto não carcinogênico, todos os poços apresentaram-se com concentrações inferiores a nova meta de remediação calculada. Como efeito colateral, foi observado o aumento das concentrações de metais dissolvidos, como: alumínio, bário, cromo e ferro. Tal mobilização de metais para a água subterrânea pode ser considerada temporária. Após o total consumo do permanganato de potássio pelos contaminantes ainda presentes no meio, as características físico-químicas do aquífero retornarão à situação identificada naturalmente, permitindo a precipitação dos metais. / Most of the currently known contaminated areas are the result of past practices, where precautions regarding protection of human health and the environment were either unknown or ignored. The indiscriminate use of chlorinated solvents is the driving factor that has led to such compounds becoming one of the main sources of contamination in the industrial sector. Chlorinated solvents are highly toxic and, when present at even low concentrations in groundwater, they make this resource unfit for human consumption. Such remediation techniques as natural attenuation, or that involve pumping and treatment of groundwater contaminated by chlorinated solvents, are currently being replaced by destructive chemical methods, as they show satisfactory results in a shorter period of time than previously used techniques. This study has the objective of showing the results obtained at two industrial sites where remediation techniques have been used involving in-situ chemical reduction, through injection of calcium polysulfide, and in-situ chemical oxidation, with injection of potassium permanganate. At both sites, organochlorine contaminants are the main compounds of concern present in groundwater. In-situ chemical reduction is a methodology that uses a chemical agent in order to reduce iron III oxides, naturally present in the sedimentary aquifer, and transform them into iron II which, in turn, reduces the organochlorine contaminants. The principal characteristic of this methodology is that of contiguous elimination of two chlorine atoms from contaminant molecules, which tends to reduce or eliminate accumulation of such toxic byproducts as vinyl chloride. In in-situ chemical oxidation, the chemical agent brings about a transfer of electrons, where the Cl- ions of contaminant molecules are replaced by H+ ions. Due to the low degree of reactivity between potassium permanganate and the aquifer matrix during chemical oxidation reactions, this oxidizing agent can be transported via groundwater flow, by advective and dispersive processes, and persist for a longer period of time, reacting with organic contaminants. Bench tests performed with contaminated saturated soil from one of the sites under study showed excellent results through the use of calcium polysulfide; however, the same results were not observed during a pilot test performed in the field. Although product dispersion was observed in the vicinity of at least one of the points where the solution had been injected, it was found that there was no significant reduction of contaminants, showing that iron II was not effective in enhancing the degradation process. This could have been the result of a series of factors, for example, possible reactions or the hydraulic or geological characteristics of the medium. Therefore, it was decided not to continue with use of this methodology as a remediation alternative for the whole impacted area, making it necessary for further studies in order to assess the best technique applicable at the site. With respect to the site where a chemical oxidation approach was adopted, remediation was considered to be effective. Over a period of twenty-two months, during which groundwater monitoring activities were performed, the presence of potassium permanganate was observed in the most impacted areas of the contamination plumes, a fact that allowed for the electron transfer process and, consequently, contaminant oxidation. Twenty-two months after initiation of injection activities, the main contaminant identified at the site (1,1-dichloroethene) was only detected at one point at a concentration exceeding the post-remediation target value established prior to commencing these activities. Considering that, during the sequence of activities related to the remediation process, this contaminant underwent changes in its toxicological values established by the United States Environmental Protection Agency, and came to be considered a non-carcinogenic compound, all wells showed concentrations below the new calculated post-remediation target. As a collateral effect, there was found to be an increase in concentrations of such dissolved metals as aluminum, barium, chromium and iron. Such mobilization of metals to groundwater can be considered a temporary effect. Following complete consumption of potassium permanganate by contaminants still present in the medium, the physical-chemical characteristics of the aquifer will return to the situation occurring naturally, allowing for the precipitation of these metals.

Recentemente, o uso de persulfato em processo de oxidação química in situ em áreas contaminadas por compostos orgânicos ganhou notoriedade. Contudo, a matriz sólida do solo pode interagir com o persulfato, favorecendo a formação de radicais livres, evitando o acesso do oxidante até o contaminante devido a oxidação de compostos reduzidos presentes no solo ou ainda pela alteração das propriedades hidráulicas do solo. Essa pesquisa teve como objetivos avaliar se as interações entre a solução de persulfato com três solos brasileiros poderiam eventualmente interferir sua capacidade de oxidação bem como se a interação entre eles poderia alterar as propriedades hidráulicas do solo. Para isso, foram realizados ensaios de oxidação do Latossolo Vermelho (LV), Latossolo Vermelho Amarelo (LVA) e Neossolo Quartzarênico (NQ) com solução de persulfato (1g/L e 14g/L) por meio de ensaios de batelada, bem como a oxidação do LV por solução de persulfato (9g/L e 14g/L) em colunas indeformadas. Os resultados mostraram que o decaimento do persulfato seguiu modelo de primeira ordem e o consumo do oxidante não foi finito. A maior constante da taxa de reação (kobs) foi observada para o reator com LV. Essa maior interação foi decorrente da diferença na composição mineralógica e área específica. A caulinita, a gibbsita e os óxidos de ferro apresentaram maior interação com o persulfato. A redução do pH da solução dos reatores causou a lixiviação do alumínio e do ferro devido a dissolução dos minerais. O ferro mobilizado pode ter participado como catalisador da reação, favorecendo a formação de radicais livres, mas foi o principal responsável pelo consumo do oxidante. Parte do ferro oxidado pode ter sido precipitado como óxido cristalino favorecendo a obstrução dos poros. Devido à maior relação entre massa de persulfato e massa de solo, a constante kobs obtida no ensaio com coluna foi 23 vezes maior do que a obtida no ensaio de batelada, mesmo utilizando concentração 1,5 vezes menor no ensaio com coluna. Houve redução na condutividade hidráulica do solo e o fluxo da água mostrou-se heterogêneo após a oxidação devido a mudanças na estrutura dos minerais. Para a remediação de áreas com predomínio de solos tropicais, especialmente do LV, pode ocorrer a formação de radicais livres, mas pode haver um consumo acentuado e não finito do oxidante. Verifica-se que o pH da solução não deve ser inferior a 5 afim de evitar a mobilização de metais para a água subterrânea e eventual obstrução dos poros por meio da desagregação dos grãos de argila. / Recently the persulfate application for in situ chemical oxidation at areas contaminated by organic compounds gained notoriety. However, the persulfate can interact with the solid matrix of the soil favoring the formation of free radicals, avoiding the oxidant access to the contaminant due to the oxidation of reduced compounds present in the soil or by changing the hydraulic properties of the soil. This research aimed to evaluate if the interactions between the persulfate solutions and three Brazilian tropical soils could eventually interfere on the persulfate oxidation capacity and if the interaction between them could modify the hydraulic properties of the soil. For such, oxidation tests were performed with soils: Latossolo Vermelho (LV), Latossolo Vermelho Amarelo (LVA) and Neossolo Quartzarênico (NQ) with persulfate solution (1 and 14 g/L) through batch tests and LV oxidation by persulfate solution (9 and 14 g/L) on undisturbed columns. The results showed that persulfate decay followed a first order model and oxidant consumption was not finite. The higher reaction rate coefficient (kobs) was observed in the reactor with LV. This higher interaction was due to the difference in the mineralogical composition and surface area. Kaolinite, gibbisita and iron oxides showed greater interaction with persulfate. The pH reduction on the reactor solution caused the aluminum and iron leaching due to dissolution of minerals. The mobilized iron may have participated as a reaction catalyst favoring the formation of free radicals although it was the major responsible for the oxidant consumption. Part of oxidized iron may have been precipitated as crystalline oxide favoring the clogged pores. As a consequence of the higher mass proportion between persulfate and soil, the kobs constant obtained in the column test was 23 times higher than the one observed on the batch test, even utilizing a concentration 1.5 times lower than bath test. There was a reduction in the soil hydraulic conductivity and the water flow proved to be heterogeneous after oxidation due to changes in minerals structure. For remediation purposes in areas with predominance of tropical soils, especially LV, the formation of free radicals may occur but an accented and not finite oxidant consumption may happen. It is verified that the pH solution should not be inferior than 5 to prevent the mobilization of metals to the groundwater and a possible pores clogging by the breakdown of the clay grains.

abstract: Mineral weathering and industrial activities cause elevated concentration of hexavalent chromium (Cr(VI)) in groundwater, and this poses potential health concern (>10 ppb) to southwestern USA. The conversion of Cr(VI) to Cr(III) – a fairly soluble and non-toxic form at typical pH of groundwater is an effective method to control the mobility and carcinogenic effects of Cr(VI). In-situ chemical reduction using SnCl2 was investigated to initiate this redox process using jar testing with buffered ultrapure water and native Arizona groundwater spiked with varying Cr(VI) concentrations. Cr(VI) transformation by SnCl2 is super rapid (<60 seconds) and depends upon the molar dosage of Sn(II) to Cr(VI). Cr(VI) removal improved significantly at higher pH while was independent on Cr(VI) initial concentration and dissolved oxygen (DO) level. Co-existing oxyanions (As and W) competed with Cr(VI) for SnCl2 oxidation and adsorption sites of formed precipitates, thus resulted in lower Cr(VI) removal in the challenge water. SnCl2 reagent grade and commercial grade behaved similarly when freshly prepared, but the reducing strength of the commercial product decreased by 50% over a week after exposing to atmosphere. Equilibrium modeling with Visual MINTEQ suggested redox potential < 400 mV to reach Cr(VI) treatment goal of 10 ppb. Kinetics of Cr(VI) reduction was simulated via the rate expression: r=-k[H+]-0.25[Sn2+]0.5[Cr2O72-]3 with k = 0.146 uM-2.25s-1, which correlated consistently with experimental data under different pH and SnCl2 doses. These results proved SnCl2 reductive treatment is a simple and highly effective method to treat Cr(VI) in groundwater. / Dissertation/Thesis / Masters Thesis Civil, Environmental and Sustainable Engineering 2019

In situ chemical oxidation (ISCO) is a leading-edge technology for soil and groundwater remediation, and involves injecting a chemical oxidant (e. g. , permanganate, hydrogen peroxide, or persulfate) into the subsurface to deplete contaminant mass through oxidation. Since the delivery of the chosen oxidant to the target treatment zone must occur in situ, the interaction between the injected oxidant and the aquifer material is a key controlling factor for a successful ISCO application. While many published ISCO studies have focused on the interaction between an oxidant and target contaminants, many questions still remain on the interaction between a potential oxidant and the aquifer material. Through a series of bench-scale experiments with aquifer materials collected from 10 sites throughout North America, the research presented in this thesis provides insight into the interaction between these aquifer materials and two widely used ISCO oxidants; permanganate and hydrogen peroxide. <br /><br /> The investigation into the interaction between aquifer materials and permanganate consisted of three series of bench-scale experiments: (1) long-term batch experiments which were used to investigate permanganate consumption in response to fundamental geochemical properties of the aquifer materials, (2) short-term batch experiments which were designed to yield kinetic data that describe the behavior of permanganate in the presence of various aquifer materials, and (3) column experiments which were used to investigate permanganate transport in a system that mimics the subsurface environment. The long-term experiments which involved more than 180 batch reactors monitored for ~300 days showed that the unproductive permanganate consumption by aquifer materials or natural oxidant demand (NOD) is strongly affected by the initial permanganate concentration, permanganate to solid mass ratio, and the reductive components associated with each aquifer material. This consumption cannot be represented by an instantaneous reaction process but is kinetically controlled by at least a fast and slow reactive component. Accordingly, an empirical expression for permanganate NOD in terms of aquifer material properties, and a hypothetical kinetic model consisting of two reaction components were developed. In addition, a fast and economical permanganate NOD estimation procedure based on a permanganate COD test was developed and tested. The investigation into short-term permanganate consumption (time scale of hours) was based on the theoretical derivation of the stoichiometric reaction of permanganate with bulk aquifer material reductive components, and consisted of excess permanganate mass experiments and excess aquifer material mass experiments. The results demonstrated that permanganate consumption by aquifer materials can be characterized by a very fast reaction on the order of minutes to hours, confirming the existence of the fast reaction component of the hypothetical kinetic model used to describe the long-term permanganate NOD observations. A typical experimental column trial consisted of flushing an aquifer-material packed column with the permanganate source solution until sufficient permanganate breakthrough was observed. The permanganate column results indicated the presence of a fast and slow consumption rate consistent with the long-term batch test data, and an intermediate consumption rate affecting the shape of the rising limb of the breakthrough curve. Finally, a comparison of the experimental results between batch and column systems indicated that permanganate NOD was significantly overestimated by the batch experiments; however, permanganate consumption displayed some similarity between the batch and column systems and hence an empirical expression was developed to predict permanganate consumption in physically representative column systems from batch reactor data. <br /><br /> The interaction between hydrogen peroxide and aquifer materials was also investigated with both batch and column experiments. A series of batch experiments consisting of a mixture of 2% hydrogen peroxide and 15 g of aquifer materials was used to capture the overall hydrogen peroxide behavior in the presence of various aquifer materials. The results indicated that the decomposition of hydrogen peroxide in the presence of various aquifer materials followed a first-order rate law, and was strongly affected by the content of amorphous transition metals (i. e. , Fe and Mn). Although hydrogen peroxide decomposition is related to the total organic carbon (TOC) content of natural aquifer materials, the results from a two-week long exposure to hydrogen peroxide suggests that not all forms of natural organic matter contributed to this decomposition. A multiple linear regression analysis was used to generate predictive relationships to estimate hydrogen peroxide decomposition rate coefficients based on various aquifer material properties. The enhanced stability of hydrogen peroxide was investigated under six scenarios with the addition of chelating reagents. The impact of a new green chelating reagent, S,S'-ethylenediaminedisuccinate (EDDS), on the stability of hydrogen peroxide in the presence of aquifer materials was experimentally examined and compared to that of the traditional and widely used chelating reagent, Ethylenediaminetetraacetic (EDTA). The results demonstrated that EDDS was able to significantly increase the stability of hydrogen peroxide, especially for aquifer materials with low TOC contents and/or high dissolvable Fe and Mn contents. Finally, to complement and expand the findings from the batch experiments, column experiments were conducted with aquifer materials from five representative sites. Each column was flushed with two types of source solutions (with or without EDDS addition) at two flow rates. The column experiments showed that the use of EDDS resulted in an earlier breakthrough and a higher stable concentration of hydrogen peroxide relative to the case without the addition of EDDS. The hydrogen peroxide decomposition rate coefficients generated from the column data were significantly higher than those generated from the batch test data and no correlation between hydrogen peroxide decomposition coefficients obtained from column and batch experiments was observed. Based on the column experimental results, a one-dimensional transport model was also calibrated to capture the hydrogen peroxide breakthrough process. <br /><br /> Data from bench-scale tests are routinely used to support both ISCO design and site screening, and therefore the findings from this study can be used as guidance on the utility of these tests to generate reliable and useful information. In general, the behavior of both permanganate and hydrogen peroxide in the presence of aquifer materials in batch and the column systems clearly indicates that the use of batch test data for ISCO system design is questionable since column experiments are believed to mimic in situ conditions better since column systems provide more realistic aquifer material contact. Thus the scaling relationships developed in this study provide meaningful tools to transfer information obtained from batch systems, which are widely employed in most bench-scale studies, to column systems.