High nitrogen discharge from the municipal wastewater is a major concern for the South Australian Government, primarily due to negative impacts on the marine environment. Therefore, under the South Australian Environmental Improvement Program, (SA EIP), all metropolitan wastewater treatment plants have been reconfigured to achieve enhanced nitrogen removal. Secondary treatment (denitrification process) at the metropolitan wastewater treatment plants must be optimised to meet the discharge guideline of 10 mg/L total nitrogen. However, secondary treatment at some plants is carbon limited (low C/N ratio), and external carbon supplementation is required to meet this discharge guideline. Molasses provides the current external carbon source at two plants. It is relatively inexpensive, but other carbon sources, particularly industrial waste streams, may be more attractive, due to the potentially lower material cost, as it is practically free, and environmentally friendly. Potato starch and sonicated return activated sludge (RAS) were considered. In this study, the bioavailability of the soluble carbon in potato starch and ultrasound treated RAS were assessed. The associated objective was to investigate the potential of both carbon sources as an external carbon donor for the denitrification zone of wastewater treatment plants to economically improve biological nitrogen removal. The economic analysis was performed using mainly United States dollars and the fixed capital investments and total capital costs were converted to Australian dollars. This was due to the United States dollars currency quotes obtained for the materials and unit operations required. SCOD from the three sources was quantified and preliminary results were presented. Molasses provided the highest SCOD release of 1.1285 x 10⁶ mg-SCOD/L, sonicated RAS produced 5.6 to 68.4 times the SCOD release of the untreated RAS (35.6 mg-SCOD/L) depending on the ultrasound intensity and treatment time, while the highest soluble carbon release obtained using potato starch was 809 mg-SCOD/L (using 20.9 g/100 mL potato starch concentration). Based on the experimental SCOD results, batch denitrification tests using the proposed carbon sources were carried out. The nitrogen removal efficiency at low dose (12.48 mg-SCOD/L) using molasses, potato starch and sonicated RAS were 77.54%, 57.24%, and 72.76% respectively, whilst at high dose (124.80 mg-SCOD/L) were 94.04%, 66.32%, and 92.10% correspondingly. In similar order of the proposed carbon sources, the nitrate removal rates for the first phase denitrification with low dose were 1.44, 1.16, and 1.18 mg-NO₃ − /h respectively, whilst the nitrate removal rate of the first phase denitrification with high dose improved to 2.01, 1.26, and 1.96 mg-NO₃ −/h correspondingly. From the denitrification test results, molasses proved to be the optimal carbon source in terms of nitrate removal. However sonicated RAS possesses similar denitrification performance and may be a suitable alternative. An economic analysis for sonicated RAS Option 2 confirmed it as the most viable substitute. The time to recover the initial investment (payback period) is approximately 6.5 years and the breakeven point is approximately 8 years. Both denitrification tests and economic analyses demonstrate that sonicated RAS may be a viable and attractive substitute for the molasses. / http://proxy.library.adelaide.edu.au/login?url= http://library.adelaide.edu.au/cgi-bin/Pwebrecon.cgi?BBID=1337059 / Thesis (M.Eng.Sc.) - University of Adelaide, School of Chemical Engineering, 2008

High nitrogen discharge from the municipal wastewater is a major concern for the South Australian Government, primarily due to negative impacts on the marine environment. Therefore, under the South Australian Environmental Improvement Program, (SA EIP), all metropolitan wastewater treatment plants have been reconfigured to achieve enhanced nitrogen removal. Secondary treatment (denitrification process) at the metropolitan wastewater treatment plants must be optimised to meet the discharge guideline of 10 mg/L total nitrogen. However, secondary treatment at some plants is carbon limited (low C/N ratio), and external carbon supplementation is required to meet this discharge guideline. Molasses provides the current external carbon source at two plants. It is relatively inexpensive, but other carbon sources, particularly industrial waste streams, may be more attractive, due to the potentially lower material cost, as it is practically free, and environmentally friendly. Potato starch and sonicated return activated sludge (RAS) were considered. In this study, the bioavailability of the soluble carbon in potato starch and ultrasound treated RAS were assessed. The associated objective was to investigate the potential of both carbon sources as an external carbon donor for the denitrification zone of wastewater treatment plants to economically improve biological nitrogen removal. The economic analysis was performed using mainly United States dollars and the fixed capital investments and total capital costs were converted to Australian dollars. This was due to the United States dollars currency quotes obtained for the materials and unit operations required. SCOD from the three sources was quantified and preliminary results were presented. Molasses provided the highest SCOD release of 1.1285 x 10⁶ mg-SCOD/L, sonicated RAS produced 5.6 to 68.4 times the SCOD release of the untreated RAS (35.6 mg-SCOD/L) depending on the ultrasound intensity and treatment time, while the highest soluble carbon release obtained using potato starch was 809 mg-SCOD/L (using 20.9 g/100 mL potato starch concentration). Based on the experimental SCOD results, batch denitrification tests using the proposed carbon sources were carried out. The nitrogen removal efficiency at low dose (12.48 mg-SCOD/L) using molasses, potato starch and sonicated RAS were 77.54%, 57.24%, and 72.76% respectively, whilst at high dose (124.80 mg-SCOD/L) were 94.04%, 66.32%, and 92.10% correspondingly. In similar order of the proposed carbon sources, the nitrate removal rates for the first phase denitrification with low dose were 1.44, 1.16, and 1.18 mg-NO₃ − /h respectively, whilst the nitrate removal rate of the first phase denitrification with high dose improved to 2.01, 1.26, and 1.96 mg-NO₃ −/h correspondingly. From the denitrification test results, molasses proved to be the optimal carbon source in terms of nitrate removal. However sonicated RAS possesses similar denitrification performance and may be a suitable alternative. An economic analysis for sonicated RAS Option 2 confirmed it as the most viable substitute. The time to recover the initial investment (payback period) is approximately 6.5 years and the breakeven point is approximately 8 years. Both denitrification tests and economic analyses demonstrate that sonicated RAS may be a viable and attractive substitute for the molasses. / http://proxy.library.adelaide.edu.au/login?url= http://library.adelaide.edu.au/cgi-bin/Pwebrecon.cgi?BBID=1337059 / Thesis (M.Eng.Sc.) - University of Adelaide, School of Chemical Engineering, 2008

Made available in DSpace on 2014-06-11T19:27:17Z (GMT). No. of bitstreams: 0 Previous issue date: 2006-12-06Bitstream added on 2014-06-13T18:55:52Z : No. of bitstreams: 1 paulino_cz_me_araca.pdf: 323136 bytes, checksum: 6854d586f088791d23b4e269a253d293 (MD5) / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP) / Rubrivivax gelatinosus é uma Bactéria Púrpura Não Sulfurosa (BPNS) que apresenta a capacidade de realizar a biorremediação de águas residuárias e, ao mesmo tempo, produzir pigmentos carotenóides. Os objetivos desse estudo foram a caracterização da curva de crescimento da bactéria no efluente de abatedouro avícola em nível de 1% (v/v) de inóculo, a determinação da produtividade do processo de obtenção de biomassa e a avaliação da capacidade de remoção da Demanda Química Oxigênio do processo. R. gelatinosus apresentou maior crescimento no oitavo dia de cultivo (Absorvância = 1.177; peso-seco = 0.18 g l-1), produtividade de 0.085 g biomassa (massa seca) l-1 d-1 e uma redução de 91% na DQO do efluente de abatedouro avícola. / Purple nonsulfur phototrophic bacterium Rubrivivax gelatinosus was used to promote the bioremediation of poultry slaugtherhouse wastewater. The aims of this study were to characterize the bacterium growth curve in that effluent at 1% (v/v) inoculum level, to determine the productivity of the biomass production process and to evaluate the Chemical Oxygen Demand removal activity of the process. R. gelatinosus showed the highest growth on the 8th day of cultivation (Absorbance = 1.177; Dry weight = 0.18 g l-1), productivity was around 0.085 g biomass (dry weight) l-1 d-1 and the COD of the poultry slaugtherhouse wastewater decreased in 91%.

Made available in DSpace on 2014-10-09T12:26:54Z (GMT). No. of bitstreams: 0 / Made available in DSpace on 2014-10-09T14:00:52Z (GMT). No. of bitstreams: 0 / Dissertacao (Mestrado) / IPEN/D / Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP

Made available in DSpace on 2014-10-09T12:26:54Z (GMT). No. of bitstreams: 0 / Made available in DSpace on 2014-10-09T14:00:52Z (GMT). No. of bitstreams: 0 / A cidade de Jundiaí está localizada a aproximadamente 60 Km de São Paulo e tem uma população de 342.983 mil habitantes sendo que 94,37% residem na zona urbana. A cidade está inserida na bacia hidrográfica do Rio Jundiaí, rio que é formado a partir da confluência do Rio Jundiaizinho com o Ribeirão das Taipas e possui uma extensão de 123 quilômetros e sua foz está situada em Salto, na confluência do Rio Jundiaí com o Rio Tietê. Está é menor bacia hidrográfica do estado de São Paulo e também uma das mais industrializadas. A cidade de Jundiaí conta com a Estação de Tratamento de Esgotos Novo Horizonte (ETE Jundiaí), que coleta 98% dos esgotos da cidade, trata 100% de todo esgoto coletado, com eficiência de remoção de 92% de carga orgânica, esgoto que depois do tratamento é lançado no Rio Jundiaí. O objetivo deste trabalho foi utilizar ensaios de toxicidade com organismos aquáticos para avaliar a carga tóxica que chega à ETE, bem como a eficiência do tratamento biológico e a influência da estação no seu entorno. Foram coletadas amostras em 6 pontos distintos; à montante da ETE (P1), na entrada da ETE (P2), na calha de distribuição das lagoas de aeração (P3), nas 2 saídas da ETE (P4 e P5) e à jusante da ETE (P6). As amostras de afluente da ETE foram mais tóxicas que os efluentes da ETE; já os resultados das amostras do rio não apresentaram diferença. Para Vibrio fischeri os valores de CE(i)50 variaram entre 2,23% e 9,39% para a calha de entrada das lagoas de aeração, enquanto que para Daphnia similis variaram entre 15,52% e 89,95%; para a entrada da ETE os valores variaram entre 4,63% e 8,31% para Vibrio fischeri , e 17,68% e não tóxico para Daphnia similis. Nas campanhas onde foram amostradas as saídas da ETE e águas do rio, os ensaios realizados com Vibrio fischeri apresentaram resultados entre 53,55% e não tóxico para águas do rio e 29,46% e não tóxico para o efluente da ETE, já para Daphnia similis, os resultados estão entre 55,92% e não tóxico para águas do rio e 70,97% e não tóxico para o efluente da ETE. Nos ensaios realizados com Ceriodaphnia dubia, a média de nascimentos para águas do rio esteve entre 4,60 e 15,00 enquanto que para o efluente da ETE esteve entre 4,50 e 10,35 para amostra bruta. Os resultados de toxicidade comprovam a eficiência da ETE na remoção de toxicidade porém outros parâmetros devem ser observados para se comprovar o impacto de seus efluentes sobre as águas do rio. / Dissertacao (Mestrado) / IPEN/D / Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP

The purpose of this Bachelor thesis was to establish a method for determining the chemical oxygen demand (COD) fractionation in wastewater from cruise liners. COD fractions of interest were soluble biodegradable (SS), particulate biodegradable (XS), soluble unbiodegradable (SI) and particulate unbiodegradable (XI). Three types of wastewater (gray water, black water and permeate) were analysed and a method with a physiochemical approach was established. The method was originally elaborated by Jun Wu et al in the study “Wastewater COD biodegradability fractionated by simple physical–chemical analysis” (2014) Chemical Engineering Journal[ES1] [JB2]  258, p 450-459. The method was also used for comparison reasons of the COD fractionation in permeate before and after advanced treatment with nanofiltration and ozonation. Total COD in permeate was almost half of the initial value after nanofiltration and XI was eliminated. After ozonation no significant difference was observed neither in total COD concentration or fractionation pattern. The conclusion is that this method to determine the COD fractions has potential but it needs further optimization in form of adjusting the methods matrix specifically based on wastewater from cruise liners. / NAUTEK

This research uses Regression analysis of fluorescence spectroscopy results to correlate with Biochemical Oxygen Demand (BOD5). Fluorescence spectroscopy was applied to samples taken from seven sample sites in the Provo and Orem waste water treatment plants found in Utah County. A total of 161 samples were collected for this research. 23 samples each were taken from four sites in the Provo waste water treatment plant namely Provo head works, aeration basin, primary filter settlement basin and the Provo effluent basin. The Orem head works, the clarifier and the Orem effluent basin were the three sample sites in the Orem waste water treatment plant where 23 samples each were collected to carry out the analysis. The fluorescent characteristics of the samples were determined using fluorescence spectrometry. These intensities were correlated with standard five day Biochemical Oxygen Demand (BOD5) values which were used as a measure of the amount of biodegradable organic material present. Chemical oxygen demand (COD) data were also taken from these treatment plants for correlation purposes. Three different correlation analyses were made which were the correlation of fluorescence spectroscopy excitation-emission matrix (EEM) against (1) individual sites BOD and COD values (2) Provo only and Orem only BOD and COD values (3) combined Provo and Orem BOD and COD values. The correlation of Individual site EEMs against BOD and COD values produced the best results. There was a higher correlation of EEM with BOD data than COD data. The R-squared for the combined Provo and Orem BOD data was 0.756 and that for COD was 0.729. Very high R-squared was obtained for Provo Influent data and Orem Influent data which were 0.955 and 0.946 respectively. This method can be used by wastewater stakeholders in deriving quick results in determining potential pollution events within a shorter time frame. This research demonstrates that there is a correlation between EEM and BOD/COD.

No description available.

Although the A-stage high-rate activated sludge (HRAS) process destroys some of the chemical energy present in municipal wastewater, this process has been gaining attention as a viable technology for achieving energy neutrality at water resource recovery facilities. In addition to carbon capture for energy recovery, A-stages are also being utilized upstream of shortcut biological nitrogen removal (BNR) processes as these BNR processes often require a controlled influent carbon to nitrogen ratio that is lower than required for conventional BNR processes. While there is extensive knowledge on conventional activated sludge processes, including process controllers and activated sludge models, there has been little detailed research on the carbon removal mechanisms of A-stage processes operated at solids retention times (SRT) less than about one day. The overall objective of this study was to elucidate the chemical oxygen demand (COD) removal mechanisms of short SRT activated sludge processes with a specific focus on the removal of the different COD fractions under varying operating conditions including dissolved oxygen, hydraulic retention time, temperature, and SRT. Once understood, automatic process control logic was developed with the purpose of producing the influent characteristics required for emerging shortcut BNR processes and capturing the remaining COD with the intent of redirecting it to an energy recovery process. To investigate the removal and assimilation of readily biodegradable substrate (SS), this study evaluated a respirometric method to estimate the SS and active heterotrophic biomass (XH) fractions of the raw wastewater influent and effluent of an A-stage pilot process. The influent SS values were comparable to the SS values determined using a physical-chemical method, but the effluent values did not correlate well. This led to the measurement of the heterotrophic aerobic yield coefficient and decay rate of the pilot process. The yield coefficient was estimated to be 0.79±0.02 gCOD/gCOD, which was higher than the accepted value of 0.67 g/g. It was speculated that the batch respirometry tests resulted in the aerobic storage of SS and this likely contributed to the error associated with the determination of SS and XH. Therefore, physical-chemical fractionation methods were used to determine the removal of the individual COD fractions. It was concluded that the SRT was the primary control parameter and below a 0.5 day SRT the dominate COD removal mechanisms were assimilation and oxidation of readily degradable substrate and sedimentation of particulate matter. At SRTs between 0.5-1 days, COD removal became a function of hydrolysis, as adsorption of particulate and colloidal matter was maximized but not complete because of limited adsorption sites. Once adequate adsorption sites were available, effluent quality became dependent on the efficiency of bioflocculation and solids separation. While the SRT of the pilot process could not be directly controlled because of severe biofouling issues when using in situ sensors, a MLSS-based SRT controller was successfully implemented instead. The controller was able to reduce total COD removal variation in the A-stage by 90%. This controller aslo provided the capability to provide a consistent carbon to nitrogen ratio to the downstream B-stage pilot process. To ascertain the settling, dewaterability, and digestibility of the sludge produced by the pilot A-stage process, several standardized and recently developed methods were conducted. The results from these tests indicated that the A-stage had similar dewaterability and digestibility characteristics to primary sludge with average achievable cake solids of 34.3±0.4% and average volatile solids reduction (VSR) of 82±4%. The A-stage sludge also had an average specific methane yield of 0.45±0.06 m3CH4/kgVS. These results were attributed to low extracellular polymeric substance (EPS) content. However, further research is needed to better quantify EPS and determine the effect of HRAS operating parameters on EPS production. Overall the A/B pilot study was able to capture 47% of the influent COD as waste sludge while only oxidizing 45% of the influent COD. Of the COD captured, the A-stage contributed over 70% as dry solids. Coupled with high sludge production, VSR, and methane yield the A/B process was able to generate 10-20% more biogas and 10-20% less dry solids after anaerobic digestion than a comparable single-sludge BNR process. / Ph. D.

No description available.