Water remediation utilizing sorption has found strong interest due to its inexpensiveness, universal nature and ease of operation. In particular, thermo-responsive sorbents consisting of N-isopropylacrylamide (NIPAAm) offer significant potential as “smart” and advanced materials to remove multiple aqueous pollutants. NIPAAm exhibits excellent thermo-responsiveness, which senses the external temperature variation and changes its swelling and sorption behaviors in a sharp and rapid manner. At the beginning of this work, an extensive review of literature has been compiled to provide a summary of NIPAAm-based thermo-responsive sorbents in water/wastewater remediation applications. Initially, we developed a novel approach to synthesize and characterize NIPAAm copolymeric hydrogels. Four different polyphenolic crosslinkers including curcumin multiacrylate (CMA), quercetin multiacrylate (QMA), 4,4’-dihydroxybiphenyl diacrylate (44BDA) and chrysin multiacrylate (ChryMA) were successfully incorporated into crosslinked hydrogels. Their temperature responsiveness and lower critical solution temperature (LCST) were characterized using swelling studies and differential scanning calorimetry (DSC). Increasing the crosslinker content resulted in a significant decrease in the swelling ratio and LCST, which was due to the increased crosslinking and hydrophobicity introduced by the polyphenolic crosslinkers. We also demonstrated the application of two sets of aforementioned crosslinked hydrogels (NIPAAm-co-CMA and NIPAAm-co-44BDA) as effective gel sorbents to capture phenol as a model contaminant. Temperature-dependent sorption was evaluated through a binding study of phenol at 10°C and 50°C. Significant enhancement in the sorption was observed at 50°C, and this can be attributed to the phase transition induced hydrophobic interactions between the copolymer gel and phenol. Moreover, the obtained hydrogels possessed facile and efficient regeneration ability in water at 10°C, without requiring harsh solvent treatment or high energy input. Building on the sorption behavior observed with crosslinked NIPAAm hydrogels, we extended the investigation to linear copolymer systems, and these were demonstrated as a temperature responsive flocculants. Here, NIPAAm copolymers consisting of 2-phenylphenol monoacrylate (2PPMA) were successfully developed as smart flocculants to remove metal oxide nanoparticles (e.g., Fe3O4, CeO2, TiO2). The incorporation of 2PPMA enhanced the flocculation at temperatures above the LCST (e.g., 50°C), which was due to the combined hydrophobicity of 2PPMA and NIPAAm. Overall, NIPAAm-based sorbents have a variety of applications in aqueous pollutant removal and are a promising class of materials for cost-effective water remediation technology.

Mercury contamination of the North Fork Holston River below Saltville, Virginia has nearly extirpated most mussel populations. Because natural recovery of these populations has not occurred, this research combined field and laboratory assessments to determine the extent of ecological impairment in the river. In situ 60-day Asian clam (Corbicula fluminea) growth studies in 2005 showed a positive correlation (p=0.03) between low clam growth and sediment mercury levels. Because of severe low flow conditions of the NFHR in late 2005 conductivity dissipation from a point source brine discharge downstream rarely reached background level (~345 µS/cm) and was observed as high as 690 µS/cm 640 m below the discharge site. In addition, conductivity doubled in the river section adjacent to the remediated Ponds 5 and 6 (rm 81.6 and 80.4). Such low flow conditions (mean flow < 50 ft3/sec) occur in the NFHR approximately every five years. This low flow situation also evidenced a thick white flocculent or floc observed to accumulate at the base of the two remediated ponds. Analysis of the flocculent determined it to be high in aluminum (1.9-38 mg/L) and iron (2.0-51.0 mg/L), well above US Environmental Protection Agency Water Quality Criteria limits (0.0087 and 1.0 mg/L, respectively); riverine sediments collected below the accumulated floc also had high levels of calcium (240,000-380,000 mg/kg) and mercury(0.62-1.7 mg/kg). Acute tests with juveniles of Villosa iris and <24-hr old Ceriodaphnia dubia were used to measure the toxicity of the brine discharge, which had a conductivity of ~ 14,000 µS/cm. Results of these tests indicated C. dubia to be more sensitive than V. iris; however, chronic toxicity test results were similar for V. iris and C. dubia. The Lowest Observed Adverse Effect Concentration (LOAEC) for mussel survivorship after 28 days was 10,000 µS/cm, while the LOAEC for growth was 5,000 µS/cm. LOAECs for the C. dubia 7-day chronic were 25 % (survivorship) and 12.5 % (reproduction), while mean conductivity at these two concentrations was 4,054 and 2,211 µS/cm, respectively. Toxicity tests conducted with Pond 6 dyke cut discharges resulted in similar lethal concentrations for C. dubia and V. iris. Forty-eight hour LC50s of these discharges ranged from 12.07-15.95 % for C. dubia, and 17.36-18.95 % for V. iris. Dyke cut discharges also exhibited exceedingly high alkaline pH (11.5-12.2), which caused 100 % mortality to C. dubia in 15 min. The Pond 5 and 6 dyke discharges are the likely source for the flocculent accumulation at the base of the two remediated pond areas. The combined effect of mercury, aluminum and iron, along with periodic fluxes of high conductivity and alkaline pH during low flow conditions may contribute to low mussel recruitment downstream of Saltville, VA. / Master of Science

Researches are done with the aim of select yeast strains that plays a differentiated role in the process of alcoholic fermentation, with the purpose of improve the performance in the ethanol production and decrease the productions costs. In this work it was studied the application of Saccharomyces cerevisiae yeasts with flocculent features in fed batch reactor. It was evaluated the fermentative capacity of six strains of flocculent yeasts. The yeast C2/00 was involved in higher productivity and yield in ethanol compared to other yeasts tested. After it was studied the alcoholic fermentation in fed batch reactor using the yeast C2/00. The fermentations were performed at 32°C and initial pH adjusted in 4.5. The process was optimized in sucrose concentration of 170 g/L, cell concentration in the inoculum of 40% (v/v) and filling time of 6 hours, it is obtaining a yield of 92.20% in relation to the theoretical one, productivity of 6.01 g/L.h and residual sucrose of 42.84 g/L in 10.5 hours of fermentative process. It was studied the influence of cells recirculation during the fermentative process and the influence of initial concentration of ethanol and substrate in inoculum on the fed batch process with the aim of improve the productivity and reduce the residual sugar. From of this study it was obtained 92.75% of yield, 9.26 g/L.h of productivity, 2.9 g/L of residual sucrose concentration and the ethanol concentration produced was 83.37 g/L in 9 hours of fermentative process. The inhibition by the substrate and product model to the kinetics of alcoholic fermentation was proposed. The parameters of model were calculated by means of nonlinear adjust to the experimental results of growth of yeast, substrate consumption and formation of product to the batch reactor. The maximum specific speed of growth was 0.103 h-1 with KI and Ks equal to 109.86 and 30.24 g/L, respectively. With the experimental results of fed batch reactor and fed batch with recycle, it can be noted a good fit to the model proposed, resulting in a maximum specific velocity of growth of 0.080 h-1 to the process in fed batch without recycle and 0.182 h-1 to the fed batch process with recycle of fermentative media. The ethanol concentration in which the production of it is completely inhibited (P max) was 110 gethanol /L , approximately 13.92% (v/v). For the result of maximum concentration of product that inhibits fully the microorganisms growth (Pmax) was 12% (v/v), corresponding to 94.8 g/L of ethanol. The specific velocity of sedimentation (SVS) to the yeast C2/00 in pH 5 was 0.240 min-1 and the sedimentation rate of the test beaker was 0.444 cm/min. The alcoholic fermentation, using the flocculent yeast Saccharomyces cerevisiae in fed batch reactor with recycle of fermentative media provided higher productivity and yields when compared to the reported data by literature, in which used batch reactor or fed batch without recycle of fermentative media. / Com o objetivo de melhorar o desempenho na produção de etanol e diminuir os custos de produção, pesquisas são realizadas no intuito de selecionar linhagens de leveduras que vêm sendo diferenciadas no processo de fermentação alcoólica. Neste trabalho estudou-se a aplicação de leveduras Saccharomyces cerevisiae com características floculantes em reator batelada alimentada. Avaliou-se a capacidade fermentativa de seis cepas de leveduras floculantes. A levedura C2/00 foi a gerou maiores produtividade e rendimento em etanol em comparação às outras leveduras testadas. Posteriormente, estudou-se a fermentação alcoólica em processo batelada alimentada utilizando a levedura C2/00. As fermentações foram realizadas a 32°C e pH inicial ajustado em 4,5. O processo foi otimizado com concentração de sacarose de 170 g/L, concentração celular no inóculo de 40% (v/v) e tempo de enchimento de 6 horas, obtendo-se um rendimento de 92,20% em relação ao teórico, produtividade de 6,01 g/L.h e sacarose residual de 42,84 g/L em 10,5 horas de processo fermentativo. Com o intuito de melhorar a produtividade e reduzir o açúcar residual foi estudada a influência da recirculação de células durante o processo fermentativo e a influência da concentração inicial de etanol e substrato no inóculo no processo em batelada alimentada. A partir deste estudo obteve-se 92,75% de rendimento, 9,26 g/L.h de produtividade, 2,9 g/L de concentração de sacarose residual e a concentração de etanol produzido foi de 83,37 g/L em 9 horas de processo fermentativo. Foi proposto o modelo de inibição pelo substrato e produto para a cinética da fermentação alcoólica. Os parâmetros do modelo foram calculados por meio de ajuste não linear aos resultados experimentais de crescimento de leveduras, consumo de substrato e formação de produto para o reator batelada. A velocidade específica máxima de crescimento foi de 0,103 h-1 com KI e Ks iguais a 109,86 e 30,24 g/L, respectivamente. Com os resultados experimentais do reator batelada alimentada e batelada alimentada com reciclo, constatou um bom ajuste do modelo proposto, resultando em uma velocidade específica máxima de crescimento de 0,080 h-1 para o processo em batelada alimentada sem reciclo e 0,182 h-1 para o processo batelada alimentada com reciclo de meio fermentativo. A concentração máxima de etanol na qual a produção do mesmo foi completadamente inibida (P máx) foi de 110 getanol /L , aproximadamente 13,92% (v/v). No entanto a concentração máxima de produto que cessa totalmente o crescimento do micro-organismo (Pmáx) foi de 12% (v/v), correspondendo a 94,8 g/L de etanol. A velocidade específica de sedimentação (VES) para a levedura C2/00 em pH 5 foi de 0,240 min-1 e a velocidade de sedimentação pelo teste da proveta foi de 0,444 cm/min. A fermentação alcoólica, utilizando a levedura floculante Saccharomyces cerevisiae em reator batelada alimentada com reciclo de meio fermentativo forneceu maior produtividade e rendimentos quando comparados a dados reportados pela literatura, nos quais utilizaram reator batelada ou batelada alimentada sem reciclo de meio fermentativo. / Doutor em Engenharia Química

M. Tech. (Biotechnology, Department of Biosciences, Faculty of Applied and Computer Sciences), Vaal University of Technology. / Reverse osmosis (RO) membranes are widely used in water purification. The presence of biofilms in water and industrial water purification systems is prevalent. As a result, biofouling which is a biofilm problem causes adverse effects on reverse osmosis process, which include flux decline, shorter membrane lifetime and an increase in energy consumption The effect of biofouling on RO membranes was investigated at a water treatment facility at Sasol, Sasolburg by investigating the quality of water purified by the RO system and the extent of fouling that is attributed to biofouling. Chemical and microbiological data was averaged based on the results obtained from water analysis and samples from a fouled membrane. Bacteriological plate counts ranged between log 1.5 to 4 cfu/ml in water samples and log 3.9 to 4.5 cfu/cm2 on biofilm from the membrane surface. Water analysis indicated a high conductivity of 121 µS/cm in the feed and 81 ppm of the TDS, whereas in the permeate conductivity was found to be around 6 µS/cm and 3.8 ppm of the TDS. This indicated that components present in the feed were retained by the membrane. This was supported by membrane autopsy which showed that the bacteria and elements found in the feedwater were also present on the membrane surface, hence contributing to fouling. An average of 33% of cellular ATP was measured on the biofilm from membrane sample, showing that the fouling bacteria are metabolically active in situ. The results clearly indicated that an important biological activity occurred at the membrane surface.