The purpose of this thesis is to evaluate the performance and cost effectiveness of a Peroxone Groundwater Treatment Plant (PGTP) designed and operated by Montgomery Watson, in support of the Defense Evaluation Support Agency's independent analysis for the United States Army Environmental Center (USAEC). Many Department of Defense installations have sites that contain groundwater contaminated with explosive materials. Primary methods for the removal of explosive materials involve the use of Granular Activated Carbon (GAC). This process, however, requires additional waste disposal and treatment of explosive laden GAC, thereby incurring additional costs. An alternate method for the treatment of contaminated groundwater involves the use of hydrogen peroxide (H2O2) in conjunction with ozone (03). This method is referred to as the Peroxone oxidation process. A demonstration of the PGTP was conducted from 19 August to 8 November, 1996, at Cornhusker Army Ammunition Plant (CAAP), Grand Island, Nebraska using a small scale version with a maximum flow rate of 25 gallons per minute. The explosive contaminants analyzed during the demonstration include 2,4,6-Trinitrotoluene (TNT), 1,3,5-Trinitrobenzene (TNB), 1,3,5-Triazine (RDX), and Total Nitrobodies. Peroxone cost effectiveness was evaluated using a 30 year life cycle cost comparison to GAC and Ultraviolet/Ozone processes

Chloramines are used for disinfection in many water treatment facilities because of their ability to provide residual protection of water supplies while minimizing the formation of disinfection-by-products. However, chloramines can impart taste and odor to the water, which can lead to customer complaints. Furthermore, the removal of monochloramine from water is essential for certain industries. Previous research at the University of Texas at Austin has demonstrated the potential of several granular activated carbons (GAC) for removal of monochloramine under conditions typical of water treatment plants. The goal of this research project is to further quantify steady-state monochloramine reduction in fixed bed reactors (FBR) with three commercially available GACs, and improve the understanding of the physical and chemical properties that influence removal. The research was divided into 3 phases: 1. A laboratory scale fixed bed reactor experiment was used to quantify steady state monochloramine removal over time. City of Austin tap water viii was used for three GAC types (Jacobi CAT, Norit CAT, Nority CNS) at pH 8 and 9. 2. Physical characterization of each GAC was performed using analysis of nitrogen adsorption isotherms. Specific surface area, pore volume, and pore distribution were determined. Chemical characterization was performed quantitatively using Boehm titrations. Qualitative analysis was performed by analyzing FTIR spectra of untreated activated carbon samples. 3. The Monochloramine Catalysis (MCAT) model was calibrated using results from the Phase 1 and 2 experiments. Simulations of full scale point of use drinking water filters were run for various empty bed contact times and influent monochloramine concentrations. These results were compared against National Sanitation Foundation monochloramine reduction certification criteria. Results show that steady state removal was achieved for all of the activated carbons tested and this removal efficiency can reach nearly 90% using a 0.75-minute empty bed contact time. This steady state performance indicated that catalysis of the monochloramine was occurring, and removal could theoretically occur for very long periods of time. The second stage of the research shows correlation between chemical characteristics (acidity and basicity) and removal efficiency. Furthermore, physical characteristics, mainly micro-porosity, were shown to largely impact performance. Finally, the MCAT model provides a reasonable estimate of steady state removal, and is used to predict full scale point of use performance. / text

No description available.

This diploma thesis deals with the efficiency and factors affecting the adsorption of AOM (Algal Organic Matter) amino acids (AAs) arginine (Arg), phenylalanine (Phe) and aspartic acid (Asp) onto granular activated carbon (GAC) Picabiol 12x40 (PIC). The efficiency of AOM AAs removal was studied in laboratory equilibrium and kinetic experiments and it was shown that the adsorption efficiency of the selected AAs is dependent on the structure of the molecule of AAs and the nature of the functional groups of their side chain, and more particularly to solution pH, which determines the nature and size and surface charge of AAs and GAC. In contrast to this, the ionic strength (IS) of solution had relatively low effect on the AAs adsorption. Arg adsorption efficiency increased with increasing pH and reached a maximum at pH 9, where AAs and GAC were oppositely charged, and this leads to attractive electrostatic interactions. In the case of Asp adsorption on PIC practically did not work. The reason is that under all experimental conditions Asp molecules and the surface of the PIC carried identical negative charge. This led to the strong electrostatic repulsion between Asp and PIC which prevented effective adsorption. In the case of Phe the adsorption decreases with increasing pH. Maximum adsorption...

Este trabalho visa avaliar o desenvolvimento microbiano e a capacidade de degradação de carbono orgânico total (COT) em quatro colunas adsorvedoras pósfiltração, em escala de bancada, em três ensaios em batelada: o primeiro de longa duração (84 dias) com afluente de água filtrada clorada com baixa concentração de COT (1,4 mg/L); o segundo de longa duração (84 dias) com afluente de solução de glicose e água filtrada clorada com concentração de COT de 6,0 mg/L e o terceiro de curta duração (21 dias) e com o mesmo afluente utilizado no segundo teste. Foi utilizado carvão ativado granular (CAG) de mesmas características nas colunas adsorvedoras, exceto as faixas de diâmetros dos grânulos, que variaram de 0,5 a 0,71 mm (coluna 1A), de 0,84 a 1,0 mm (coluna 1B) e de 1,0 a 1,19 mm (coluna 1C) nas três colunas que tinham o diâmetro interno de 1,2 cm. A coluna 2, com diâmetro interno de 2,1 cm, recebeu CAG com grânulos na mesma faixa de diâmetros da coluna 1B (0,84 a 1,0 mm). As eficiências de remoção de COT no primeiro ensaio foram bem menores (46 a 74%) do que aquelas dos ensaios 2 (94 a 97%) e 3 (96 a 97%). Estes últimos apresentaram grande desenvolvimento da microbiota e elevadas eficiências de remoção de COT, devido ao co-metabolismo e biorregeneração nas colunas pela introdução da glicose. Nas três colunas de mesmo diâmetro, foi observado que quanto menor a faixa de diâmetros dos grânulos de CAG, maior foi o desenvolvimento da microbiota (expresso em contagens de bactérias heterotróficas); e nas colunas com mesma faixa de diâmetros de CAG e com diferentes diâmetros de coluna (1B e 2), o desenvolvimento da microbiota foi muito semelhante nos ensaios de longa duração. Com relação às eficiências de remoção de COT, não houve diferença significativa entre as quatro colunas nos ensaios de longa e curta duração com adição de glicose; no ensaio de longa duração sem adição de glicose as colunas 1A e 2 apresentaram melhores resultados em relação às demais e não há uma explicação clara para tal fato. / The major purpose of this experimental work was to evaluate the microbial development and the capabilities of degradation of Total Organic Carbon (TOC) of four post-filtration adsorption columns operated as batch reactors in three bench scale tests. The firs batch column testing was conducted by means of one long duration runs (84 days each) and the columns were fed with filtered, chlorinated water with low COT concentration (1.4 mg/L). The second batch column testing was conducted by means of one long duration runs (84 days each) and the columns were fed with a glucose and filtered chlorinated water solution (resulting TOC = 6.0 mg/L). The third batch column testing was conducted by means of one short duration runs (21 days each) and the columns were fed with the same solution of the second batch column testing. The same type of Granular Activated Carbon (GAC) was employed in all columns, except for the average granule diameter ranges. They were 0.5 to 0.71 mm (column 1A), 0.84 to 1.0 mm (column 1B), and 1.0 to 1.19 mm (column 1C), for the 12 mm diameter columns. The 21 mm diameter column 2 had CAG granules with the same size range of column 1B (0.84 to 1.0 mm). The TOC removal efficiencies in the first batch column testing were lower (46 to 74%) than 2 (94 to 97%) and 3 (96 to 97%) batch column testing. The lasts batch column testing led to high microbial growth and high TOC removal efficiencies due to cometabolism and bioregenation in the columns fed with a glucose. Regarding the three columns with the same diameter, it was observed that the lower the GAC granule size range, the higher the microbial growth rate (expressed as heterotrophic plate count); the columns with the same GAC size range but different column diameters (columns 1B and 2) the microbial growth rates were very similar with respect to the long period runs. With respect to the TOC removal efficiencies, there were no significant differences between the four columns in the long duration test runs and the short duration runs with glucose addition; in the long duration run without glucose addition, columns 1A and 2 were much more efficient at removing TOC than the other column; there is no clear explanation for it.

Este trabalho visa avaliar o desenvolvimento microbiano e a capacidade de degradação de carbono orgânico total (COT) em quatro colunas adsorvedoras pósfiltração, em escala de bancada, em três ensaios em batelada: o primeiro de longa duração (84 dias) com afluente de água filtrada clorada com baixa concentração de COT (1,4 mg/L); o segundo de longa duração (84 dias) com afluente de solução de glicose e água filtrada clorada com concentração de COT de 6,0 mg/L e o terceiro de curta duração (21 dias) e com o mesmo afluente utilizado no segundo teste. Foi utilizado carvão ativado granular (CAG) de mesmas características nas colunas adsorvedoras, exceto as faixas de diâmetros dos grânulos, que variaram de 0,5 a 0,71 mm (coluna 1A), de 0,84 a 1,0 mm (coluna 1B) e de 1,0 a 1,19 mm (coluna 1C) nas três colunas que tinham o diâmetro interno de 1,2 cm. A coluna 2, com diâmetro interno de 2,1 cm, recebeu CAG com grânulos na mesma faixa de diâmetros da coluna 1B (0,84 a 1,0 mm). As eficiências de remoção de COT no primeiro ensaio foram bem menores (46 a 74%) do que aquelas dos ensaios 2 (94 a 97%) e 3 (96 a 97%). Estes últimos apresentaram grande desenvolvimento da microbiota e elevadas eficiências de remoção de COT, devido ao co-metabolismo e biorregeneração nas colunas pela introdução da glicose. Nas três colunas de mesmo diâmetro, foi observado que quanto menor a faixa de diâmetros dos grânulos de CAG, maior foi o desenvolvimento da microbiota (expresso em contagens de bactérias heterotróficas); e nas colunas com mesma faixa de diâmetros de CAG e com diferentes diâmetros de coluna (1B e 2), o desenvolvimento da microbiota foi muito semelhante nos ensaios de longa duração. Com relação às eficiências de remoção de COT, não houve diferença significativa entre as quatro colunas nos ensaios de longa e curta duração com adição de glicose; no ensaio de longa duração sem adição de glicose as colunas 1A e 2 apresentaram melhores resultados em relação às demais e não há uma explicação clara para tal fato. / The major purpose of this experimental work was to evaluate the microbial development and the capabilities of degradation of Total Organic Carbon (TOC) of four post-filtration adsorption columns operated as batch reactors in three bench scale tests. The firs batch column testing was conducted by means of one long duration runs (84 days each) and the columns were fed with filtered, chlorinated water with low COT concentration (1.4 mg/L). The second batch column testing was conducted by means of one long duration runs (84 days each) and the columns were fed with a glucose and filtered chlorinated water solution (resulting TOC = 6.0 mg/L). The third batch column testing was conducted by means of one short duration runs (21 days each) and the columns were fed with the same solution of the second batch column testing. The same type of Granular Activated Carbon (GAC) was employed in all columns, except for the average granule diameter ranges. They were 0.5 to 0.71 mm (column 1A), 0.84 to 1.0 mm (column 1B), and 1.0 to 1.19 mm (column 1C), for the 12 mm diameter columns. The 21 mm diameter column 2 had CAG granules with the same size range of column 1B (0.84 to 1.0 mm). The TOC removal efficiencies in the first batch column testing were lower (46 to 74%) than 2 (94 to 97%) and 3 (96 to 97%) batch column testing. The lasts batch column testing led to high microbial growth and high TOC removal efficiencies due to cometabolism and bioregenation in the columns fed with a glucose. Regarding the three columns with the same diameter, it was observed that the lower the GAC granule size range, the higher the microbial growth rate (expressed as heterotrophic plate count); the columns with the same GAC size range but different column diameters (columns 1B and 2) the microbial growth rates were very similar with respect to the long period runs. With respect to the TOC removal efficiencies, there were no significant differences between the four columns in the long duration test runs and the short duration runs with glucose addition; in the long duration run without glucose addition, columns 1A and 2 were much more efficient at removing TOC than the other column; there is no clear explanation for it.

Neonicotinoid insecticides are widespread in surface waters across the agriculturally-intensive Midwestern US. We report for the first time the presence of three neonicotinoids in finished drinking water and demonstrate their general persistence during conventional water treatment. Periodic tap water grab samples were collected at the University of Iowa over seven weeks in 2016 (May-July) after maize/soy planting. Clothianidin, imidacloprid, and thiamethoxam were ubiquitously detected in finished water samples and ranged from 0.24-57.3 ng/L. Samples collected along the University of Iowa treatment train indicate no apparent removal of clothianidin and imidacloprid, with modest thiamethoxam removal (~50%). In contrast, the concentrations of all neonicotinoids were substantially lower in the Iowa City treatment facility finished water using granular activated carbon (GAC) filtration. Batch experiments investigated potential losses. Thiamethoxam losses are due to base-catalyzed hydrolysis at high pH conditions during lime softening. GAC rapidly and nearly completely removed all three neonicotinoids. Clothianidin, hydrolysis products of thiamethoxam and known metabolites of imidacloprid are susceptible to reaction with free chlorine and may undergo transformation during chemical disinfection via chlorination or during distribution with chlorine residual. We identify several transformation products resulting from these oxidation and hydrolysis reactions, and discuss implications for human health. Our work provides new insights into the persistence of neonicotinoids and their potential for transformation during water treatment and distribution, while also identifying GAC as a potentially effective management tool to lower neonicotinoid concentrations in finished drinking water.

A vast number of sites that have been contaminated by industrial activities have been identified worldwide. Many such sites now pose serious risks to humans and the environment. Given the large number of contaminated sites there is a great need for efficient, cost-effective  remediation methods. Extensive research has therefore been focused on the development of such methods. However, the remediation of old industrial sites is challenging, for several reasons. One major  problem is that organic contaminants become increasingly strongly sequestered as they persist in the soil matrix for a long period of time. This process is often referred to as ‘aging’, and leads to decreasing availability of the contaminants, which also affects the remediation efficiency. In the work underlying this thesis, the influence of soil and contaminant properties on the efficiency of various physical and chemical soil remediation methods was investigated. The investigated contaminants were polycyclic aromatic hydrocarbons (PAHs), polychlorinated dibenzo-p-dioxins (PCDDs) and dibenzofurans (PCDFs). Briefly, the results show that as the size of soil particles decreases the contaminants become more strongly sorbed to the soil’s matrix, probably due to the accompanying increases in specific surface area. This affected the efficiency of the removal of organic pollutants by both a process based on solvent washing and processes based on chemical oxidation. The sorption strength is also affected by the hydrophobicity of the contaminants. However, for a number of the investigated PAHs their chemical reactivity was found to be of greater importance for the degradation efficiency. Further, the organic content of a soil is often regarded as the most important soil parameter for adsorption of hydrophobic compounds. In these studies the effect of this parameter was found to be particularly pronounced for the oxidation of low molecular weight PAHs, but larger PAHs were strongly adsorbed even at low levels of organic matter. However, for these PAHs the degradation efficiency was positively correlated to the amount of degraded organic matter, probably due to the organic matter being oxidized to smaller and less hydrophobic forms. The amount of organic matter in the soil had little effect on the removal efficiency obtained by the solvent-washing process. However, it had strong influence on the performance of a subsequent, granular activated carbon-based post-treatment of the washing liquid. In conclusion, the results in this thesis show that remediation of contaminated soils is a complex process, the efficiency of which will be affected by the soil matrix as well as the properties of the contaminants present at the site. However, by acquiring thorough knowledge of the parameters affecting the treatability of a soil it is possible to select appropriate remediation methods, and optimize them in terms of both remediation efficiency and costs for site- and contaminant-specific applications.

<p>Analytical analyses conducted at the Himmerfjärden WWTP (285.000 PE connected) identified 70 pharmaceutical compounds belonging to different therapeutic classes. Such organic micropollutants at low detected concentration range of µg - ng l^-1 did not affect the treatment processes at WWTP. Results from analytical studies indicated continuous discharge of organic micropollutants to the surface water with a calculated load amounting to 1.51 kg day-1. Metoprolol, carbamazepine and naproxen were chosen for testing different removal methods. Oxygen Uptake Rate (OUR) tests were conducted to assess the bacterial activity of an activated sludge taken from a full scale aeration plant with the presence of selected target compounds.</p><p>A semi-technical scale membrane bioreactor ZeeWeed10™, treating final effluent from the Himmerfjärden WWTP (Sweden) was seeded with activated sludge from full scale biological stage. The membrane bioreactor (MBR) system placed after the final treatment appeared to be an insufficient technology for removal of residual amounts of organic micropollutants from WWTP effluents. Batch test studies with activated sludge taken from the membrane bioreactor and with application of granular activated carbon (GAC) filtration resulted in giving an overall assessment of removal efficiency. Metoprolol and carbamazepine tend to be resistant to the biodegradation process and in the dosed high concentration lead to bacterial cell decomposition in the activated sludge. Apparently, removal efficiency for naproxen exceeded the value of 46% with the spiked initial amount of 3.3 mg NAP g^-1MLSS. Application of the GAC filtration proved to be an efficient technique for removal of pharmaceutical compounds from treated wastewater.</p><p>Application of the statistical programme Modde7 was a time saving tool in studies of fouling occurrence. The effect of fouling phenomenon, which is a highly limiting factor for MBR performance, was minimised by adjusting the operational parameters as predicted by the Modde7 programme.</p>

The ubiquity of pharmaceuticals and personal care products in water systems is well known. With the increasing implementation of water reuse schemes in the US, concern about potential health effects of these compounds in humans has risen. While potential synergistic effects of chronic low doses exposure to a cocktail of these compounds is still being studied, it is prudent to monitor and attenuate these trace organic compounds (TOrCs) from our water sources. This research initially focused on identifying suitable `indicator' TOrCs based on theoretical physico-chemical parameters and actual experimental data. It was concluded that an indicator list will be specific to the goal targeted with dependence on treatment process, occurrence and analytical ease. Quantification of these TOrCs are part per trillion levels in water requires accurate, precise and robust analytical techniques. The next part of this research was spent on developing three different analytical methods with LC-MS/MS for the sensitive detection of TOrCs in several different water matrices including raw sewage and final drinking water. The treatment efficacy of granular activated carbon for attenuation of TOrCs is studied in detail with emphasis on developing correlations between TOrC removal and bulk organic parameters of water like UV absorbance and fluorescence by using rapid small-scale column testing. The results indicate a correlation between removal of TOrCs and bulk organic parameters that is independent of water quality. The effectiveness of commercially available activated carbon based point-of-use (POU) devices for removal of a set of TOrCs from water was evaluated. The data indicated that POUs are a viable option for treatment of TOrCs but specific removal depends on type of device, water quality and amount of water treated. Finally, further research was targeted at identifying transformation products as a result of oxidation of polyfluorinated precursor materials in reclaimed waters. The results illustrated that toxic perfluorocarboxylic acids can be formed on oxidation of fluorotelomer unsaturated carboxylic acids that are known to be present in water.