Water treatment residues (WTRs), which are by-products from the production of potable water, are chemically benign, inorganic materials which are suitable for disposal by land application. Their high phosphorus (P) sorption capacities have, however, generated some concern in an agronomic context where P is recognised as a growth limiting plant nutrient. The extent to which labile P pools are reduced or enhanced by WTR amendments is, therefore, a central issue with respect to their disposal by land application. Therefore, the aim of this study was, through the use of empirical adsorption isotherm equations and chemical fractionation of P within the residues, to investigate the chemical processes responsible for the retention and release of P from 15 South African WTRs. Chemical characterisation revealed considerable variation in residue properties relevant to P sorption-desorption processes. pH, exchangeable Ca and organic carbon content ranged from 4.77 to 8.37, 238 to 8 980 mg kg-1 and 0.50 to 11.6 %, respectively. Dithionate, oxalate and pyrophosphate extractable Al fractions ranged from 741 to 96 375, 1 980 to 82 947 and 130 to 37 200 mg kg-1, respectively. Dithionate, oxalate and pyrophosphate extractable Fe ranged from 441 to 15 288, 3 865 to 140 569 and 230 to 90 000 mg kg-1 respectively. Therefore mechanisms of retention were hypothesised to be residue specific, being dependent on the unique chemical properties of the sorbent. Elevated Ca and amorphous Al and Fe concentrations did, nevertheless, suggest that all residues had the capacity to adsorb high amounts of P and to retain this P in forms unavailable for plant uptake. These arguments were confirmed by the sorption study where labile P was, for all residues, found to constitute a small fraction of total applied P even at high application concentrations (128 mg P L-1). Sequential P fractionation revealed that most of the inherent P (which ranged from 1 149 to 1 727 mg P kg-1) and applied P were retained in highly resistant mineral phases or fixed within the organic component. Thus P replenishment capacities were restricted even though residual P concentrations were often within adequate ranges for plant growth. Phosphorus adsorption data was described by four empirical adsorption isotherm equations in an effort to determine possible mechanisms of retention. Sorption data was, for most of the WTRs, described by the Temkin isotherm while the Freundlich and linear models fitted data for two residues each. A key finding was that the distribution coefficient (Kd) tended to increase with the quantity of P adsorbed (S) as opposed to decrease or remain constant in accordance with model assumptions. Therefore, the models could not be used for mechanistic interpretation, even though they provided excellent descriptions of the data. The direct relationship between Kd and S suggested a mechanism of retention involving the activation of sorption sites. This notion was supported by the fractionation study which showed that P addition results in the transfer of an increasing quantity of organically bound P to resistant residual forms. Model affinity parameters were strongly correlated to dithionate and pyrophosphate extractable Al and Fe which suggested that P was adsorbed primarily through ligand exchange mechanisms. The mobility of P bound to organic fractions did indicate that P was retained through weaker forces of attraction such as monodentate ligand exchange, charge neutralisation or proton transfer. Evidence to support the notion that P is immobilised through the formation of Ca phosphates was lacking. Based on P fractionation data, it was suggested that strong chemisorption mechanisms and the diffusion of P into WTR micropores were largely responsible for the minimal quantity of P desorbed by disequilibria desorption processes. A greater quantity of P was desorbed in the presence of oxalate and citrate which suggested that plants may increase bio-available pools through the release of organic ligands. Phosphorus desorbed in the presence of these ligands did, however, decline with P addition which confirmed that the affinity of the WTR surface for P increases with P application. Therefore, it was concluded that the application of P to WTRs is an uneconomical process unless sorption sites are already saturated or immobilisation processes are inhibited. In light of these findings, it was suggested that the absence of plant P deficiencies under the field application of WTRs is due primarily to inhibited sorption. / Thesis (M.Sc.)-University of KwaZulu-Natal, Pietermaritzburg, 2009.

Water treatment residue (WTR), a by-product of the water treatment process, consists primarily of precipitated hydroxides of the coagulants used in the water treatment process, along with sand, silt, clay, humic compounds, and dissolved organic matter. It is usually disposed of by landfill, a technology with numerous problems that include dwindling landfill capacity, extensive dewatering requirements for the WTRs, high costs of transportation, and potential liability for landfill clean-up. Therefore, land disposal (or land treatment) presents a popular alternative disposal method based on the principle that the physical, chemical, and microbial properties of the soil can be used to assimilate applied waste without inducing any negative effects on soil quality. The objective of this study was to investigate the effects of land disposal of the WTR generated by Umgeni Water, a local water treatment authority, on soil quality. These effects were investigated using depth samples from soil profiles of Westleigh and Hutton soil forms at field trials located at Ukulinga Research Farm, near Pietermartizburg and Brookdale Farm, Howick, KwaZulu-Natal, South Africa, respectively. Four rates of WTR (0, 80, 320, and 1280Mg ha-1 incorporated into the soil) were investigated at both trials, in addition to mulched treatments at rates of 320 and 1280Mg ha-1 at Brookdale only. Sampling of plots was carried out in September 2001 and May 2002, and all treatments were investigated under fallow and grassed cultivation. Laboratory measurements used to assess soil quality included pH, electrical conductivity (EC), organic carbon (QC), and microbial activity using f1uorescein diacetate (FDA) hydrolysis. At both trials in September 2001 WTR-amended plots displayed higher pH in the 0-200mm soil in comparison to the controls, whereas by May 2002 pH had returned to the condition of the controls. Addition of WTR at Ukulinga resulted in higher QC in September 2001, but in May 2002 this was similar to the controls. However, at Brookdale QC was unaffected by WTR. At Ukulinga and Brookdale the effect of WTR on EC was variable, and microbial activity in the soil profile was unaffected by WTR addition. Observations at Ukulinga and Brookdale reflected long term changes (3 and 5 years, respectively) to soil quality following WTR addition. To examine the initial changes in soil quality a laboratory experiment was set up using the field trial soils. Research objectives were also extended to include WTRs from Rand Water (Johannesburg), Midvaal Water Company (Stilfontein), Amatola Water (East London), and two samples from the Faure Water Treatment Plant (near Cape Town). The second Faure sample (Faure2 ) was collected when blue green algal problems were experienced at the plant. The measurements used to investigate these short term effects on soil quality were soil pH, EC, and microbial activity as indicated by respiration rate. Each of the WTRs added to the Hutton and Westleigh soils increased soil pH by varying increments, and the higher the WTR application rate, the higher was the pH recorded. With the exception of the Rand and Umgeni WTRs that clearly increased soil EC, the effect of the otherWTRs on EC was variable. The Faure1 and Amatola WTRs appeared to have no effect on microbial activity, whereas the Umgeni, Rand, Midvaal, and Faure2 WTRs stimulated microbial activity by Day 2 following the addition of WTR, but this had declined by Day 14. As for pH, higher microbial activity was recorded at higher WTR application rates. Changes in microbial community structure of the Hutton soil only, following the addition of WTR were examined using denaturing gradient gel electrophoresis (DGGE) analysis. Community profiles of the different WTRs proved to be markedly different. However, WTR-amended soil retained banding patterns consistent with the control soil indicating that dominant populations in the Hutton soil had been retained. The field trials indicated that long term effects of land disposal of WTR were not detrimental to the measured indicators of soil quality namely, pH, EC, QC, and microbial activity. The laboratory assessments of the short term response of the Hutton and Westleigh soil forms to WTR addition suggested that the tested variables were altered by WTR, but not significantly changed to the detriment of soil quality. Microbial community analysis indicated that the community structure of the Hutton soil was not significantly altered by WTR amendments. Present findings provide no evidence to suggest that land disposal of WTR is detrimental to soil quality. It is therefore regarded as a feasible disposal option although there are some aspects that should be investigated further. These include investigations into rhizosphere/microbial interactions and the feasibility of growing cash crops. / Thesis (M.Sc.)-University of Natal, Pietermaritzburg, 2003.

Water treatment residues (WTRs) are the by-product from the production of potable water. They consist mainly of the precipitated hydrous oxides of the treatment chemicals, and materials removed from the raw water. This study investigated the range of treatment processes and residues produced in South Africa, and two WTRs were selected for testing on selected soils and mine materials. A questionnaire was developed and sent to water treatment authorities across South Africa. Information on the treatment chemicals, dosages, volumes and current disposal practices, and a sample of WTR from each treatment plant were requested. Eleven, of 21 authorities, returned completed questionnaires, representing 37 water treatment facilities. Organic polymers were the most commonly used treatment chemical, with most plants also using lime. Other less frequently used chemicals and additives were Alz(S04)3.14I-hO, Fe2(S04)3, FeC!), sodium aluminate, activated silica, activated charcoal, CO2 and bentonite. Information given regarding residue thickening and disposal was poor. Samples from Rand Water, Umgeni Water (Midmar), Midvaal Water Company, Amatola Water and Cape Metropolitan Council (Faure) were received or collected. An additional sample from Faure was also received, representing a change in the treatment process. These samples were analysed for a range of chemical and physical characteristics. These analyses showed that the WTRs had the potential to supply some plant nutrients (Ca, Mg, Fe, S) but that metal toxicity may be a problem, in particular Mn in the Faure WTR, and that P adsorption may be severe. The samples selected to test the potential for land disposal were from Rand Water and Faure. A pot experiment tested the growth of Eragrostis tefJ, Cenchrus ciliaris and Digitaria eriantha in mixtures of Rand WTR and material from a coal mine i.e., a sandy soil material, spoil material and coal combustion ash, at rates of 0, 50, 100, 200 and 400 g kg" with a uniform fertiliser treatment applied to all mixtures. The grass was harvested on three occasions and the mean total yield (dry mass) determined, as well as nutrient uptake. The pots were leached after each harvest and the pH and electrical conductivity determined. The soil, spoil and ash were characterised and pH, EC and water retention characteristics of the mixtures determined. Growth of the grasses in the ash treatments was poor and these were terminated. Eragrostis tefJ grown in the soil showed a decrease in mean total yield with increasing WTR application rate, but yield was good up to the 200 g kg" treatment at the first harvest, declining substantially by the second harvest. In general C. ciliaris and D. eriantha grown in the soil showed a decrease in mean total yield for all harvests with increasing WTR application. The yield of E. /ejJ, grown in the spoil, increased up to 100 g kg,l WTR addition, but decreased thereafter. Digitaria eriantha showed a decrease in yield, and C. ciliaris an increase, with increasing WTR application rate , but for all treatments the differences were non-significant. The pH and EC of the leachates generally increased with increasing WTR addition. The concentration of nutrients in the grasses did not indicate any deficiencies or toxicities. As the growth of grass was poor in the ash treatments, another pot experiment was established to test the growth of two creeping grass species grown in the Rand WTR as a cover over the ash material. Cynodon dactylon and Stenotaphrum secundatum were grown in 20, 40 and 60 mm layers of Rand WTR, with and without a fertiliser treatment. Both species performed best in the 60 mm layer with fertiliser, and C. dactylon performed better than S. secundatum. The former species was more tolerant of the high pH, but both have potential as cover vegetation on the ash dumps when these are covered with Rand WTR. A further glasshouse study investigated the effect of Faure WTR mixed with a nutrient poor sandy soil on the nutrient uptake and seed yield of common dry beans (Phaseolus vulgaris). The WTR was added to the soil at 0, 50, 100, 200 and 400 g kg" each with five levels of fertiliser (0, 25, 50, 100 (recommended optimum) and 150 %). Bean pods were harvested once the plants had senesced. The number of pods and mass and number of seeds per treatment were determined. The seeds were analysed for nutrient uptake. Interveinal chlorosis and necrotic lesions were evident on cotylendonous and new leaves in the WTR treated soils, the severity of the symptoms increasing with increasing rate of WTR. Additional pots were established at the 400 g kg" rate (without fertiliser) and leaf material collected for chemical analysis. This showed that Mn toxicity was the cause, with leaf concentrations about 12 times the recommended 100 mg kg" upper limit. However, mass of bean seed was highest in the 400 g kg" Faure WTR treatment with 150 % fertiliser. Nutrient translocation to the seed seemed to be relatively consistent regardless of treatment, with little accumulation ofMn. The data collected illustrated the range of conditions and types of WTRs produced in South Africa, and that in some instances these residues have favourable characteristics for land application. The use of the Rand WTR showed that it could be applied to the spoil medium at relatively high concentrations without severely negatively impacting on grass growth, but more caution should be used when applying this material to the soil medium. While the grass did not grow in the ash treatments, it would seem that with suitable species the Rand WTR could be beneficially applied to ash material as a cover layer. The use of the Faure WTR on a sandy soil seemed to potentially improve the yield of the indicator crop, but caution should be exercised due to the possibility of Mn toxicity. The use of additional fertiliser would seem to be essential. Further research would require that field scale investigation of both WTRs be conducted, as well as further studies of applicat ion rates and techniques in laboratory and glasshouse investigations. / Thesis (M.Sc.)-University of Natal, Pietermaritzburg, 2003.

Water treatment residues (WTRs) are the by-product from the production of potable water. They consist mainly of the precipitated hydrous oxides of the treatment chemicals, and materials removed from the raw water. This study investigated the range of treatment processes and residues produced in South Africa, and two WTRs were selected for testing on selected soils and mine materials. A questionnaire was developed and sent to water treatment authorities across South Africa. Information on the treatment chemicals, dosages, volumes and current disposal practices, and a sample of WTR from each treatment plant were requested. Eleven, of 21 authorities, returned completed questionnaires, representing 37 water treatment facilities. Organic polymers were the most commonly used treatment chemical, with most plants also using lime. Other less frequently used chemicals and additives were A12(SO4)3.14H2O, Fe2(SO4)3, FeC1), sodium aluminate, activated silica, activated charcoal, CO2 and bentonite. Information given regarding residue thickening and disposal was poor. Samples from Rand Water, Umgeni Water (Midmar), Midvaal Water Company, Amatola Water and Cape Metropolitan Council (Faure) were received or collected. An additional sample from Faure was also received, representing a change in the treatment process. These samples were analysed for a range of chemical and physical characteristics. These analyses showed that the WTRs had the potential to supply some plant nutrients (Ca, Mg, Fe, S) but that metal toxicity may be a problem, in particular Mn in the Faure WTR, and that P adsorption may be severe. The samples selected to test the potential for land disposal were from Rand Water and Faure. A pot experiment tested the growth of Eragrostis teff, Cenchrus ciliaris and Digitaria eriantha in mixtures of Rand WTR and material from a coal mine i.e., a sandy soil material, spoil material and coal combustion ash, at rates of 0, 50, 100, 200 and 400 g kg-1 with a uniform fertiliser treatment applied to all mixtures. The grass was harvested on three occasions and the mean total yield (dry mass) determined, as well as nutrient uptake. The pots were leached after each harvest and the pH and electrical conductivity determined. The soil, spoil and ash were characterised and pH, EC and water retention characteristics of the mixtures determined. Growth of the grasses in the ash treatments was poor and these were terminated. Eragrostis teff grown in the soil showed a decrease in mean total yield with increasing WTR application rate, but yield was good up to the 200 g kg-1 treatment at the first harvest, declining substantially by the second harvest. In general C. ciliaris and D. eriantha grown in the soil showed a decrease in mean total yield for all harvests with increasing WTR application. The yield of E. teff, grown in the spoil, increased up to 100 g kg-1 WTR addition, but decreased thereafter. Digitaria eriantha showed a decrease in yield, and C.ciliaris an increase, with increasing WTR application rate, but for all treatments the differences were non-significant. The pH and EC of the leachates generally increased with increasing WTR addition. The concentration of nutrients in the grasses did not indicate any deficiencies or toxicities. As the growth of grass was poor in the ash treatments, another pot experiment was established to test the growth of two creeping grass species grown in the Rand WTR as a cover over the ash material. Cynodon dactylon and Stenotaphrum secundatum were grown in 20, 40 and 60 mm layers of Rand WTR, with and without a fertiliser treatment. Both species performed best in the 60 mm layer with fertiliser, and C. dactylon performed better than S. secundatum. The former species was more tolerant of the high pH, but both have potential as cover vegetation on the ash dumps when these are covered with Rand WTR. A further glasshouse study investigated the effect of Faure WTR mixed with a nutrient poor sandy soil on the nutrient uptake and seed yield of common dry beans (Phaseolus vulgaris). The WTR was added to the soil at 0, 50, 100, 200 and 400 g kg-1 each with five levels of fertiliser (0, 25, 50, 100 (recommended optimum) and 150 %). Bean pods were harvested once the plants had senesced. The number of pods and mass and number of seeds per treatment were determined. The seeds were analysed for nutrient uptake. Interveinal chlorosis and necrotic lesions were evident on cotylendonous and new leaves in the WTR treated soils, the severity of the symptoms increasing with increasing rate of WTR. Additional pots were established at the 400 g kg-1 rate (without fertiliser) and leaf material collected for chemical analysis. This showed that Mn toxicity was the cause, with leaf concentrations about 12 times the recommended 100 mg kg-1 upper limit. However, mass of bean seed was highest in the 400 g kg-1 Faure WTR treatment with 150 % fertiliser. Nutrient translocation to the seed seemed to be relatively consistent regardless of treatment, with little accumulation of Mn. The data collected illustrated the range of conditions and types of WTRs produced in South Africa, and that in some instances these residues have favourable characteristics for land application. The use of the Rand WTR showed that it could be applied to the spoil medium at relatively high concentrations without severely negatively impacting on grass growth, but that more caution should be used when applying this material to the soil medium. While the grass did not grow in the ash treatments, it would seem that with suitable species the Rand WTR could be beneficially applied to ash material as a cover layer. The use of the Faure WTR on a sandy soil seemed to potentially improve the yield of the indicator crop, but caution should be exercised due to the possibility of Mn toxicity. The use of additional fertiliser would seem to be essential. Further research would require that field scale investigation of both WTRs be conducted, as well as further studies of application rates and techniques in laboratory and glasshouse investigations. / Thesis (M.Sc.)-University of Natal, Pietermaritzburg, 2003.

Grande parte do lodo gerado em ETAs no Brasil ainda é disposta em rios ou em aterros sanitários. Contudo, principalmente em grandes centros urbanos, condições de licenciamento ambiental restritivas e custos logísticos crescentes tem levantado interesse em usos benéficos para esse resíduo. Um obstáculo para a mudança de paradigma recai no fato de que muito raramente operadores e projetistas de ETAs nacionais conseguirem prever, com algum grau de confiabilidade, a massa e volume de resíduos produzidos pelo tratamento da água bruta. Geralmente, usa-se para esse fim fórmulas empíricas, que relacionam a produção de lodo à concentração de sólidos em suspensão totais (SST) na água bruta e à dosagem de produtos químicos. Os objetivos deste trabalho são: comparar o desempenho de dois dos principais métodos quantitativos de estimativa de produção de lodo o método de fórmulas empíricas, e o do balanço de massa; investigar a prática disseminada de se estimar a concentração de sólidos em suspensão totais na água bruta por meio de modelos de regressão linear com a turbidez como variável independente; e delinear condições para a aplicação dessa correlação. Foram utilizados dados de seis ETAs de ciclo completo operadas pela SABESP (ABV, Alto Cotia, Cubatão, Guaraú, Franca e Presidente Prudente), além de dados de monitoramento de 130 estações de monitoramento de águas superficiais da CETESB. Os resultados sugerem que a identificação de correlações significativas entre concentração de SST e turbidez é elusiva, e não constitui tarefa trivial. Do universo de 130 estações da CETESB, somente 7 apresentaram correlação significativa; das ETAs, somente Presidente Prudente. Modelos de regressão alternativos utilizando outras variáveis (cor, vazão média mensal e mês), combinadas com a turbidez ou isoladamente, foram desenvolvidos. Somente a inclusão do mês como variável categórica foi capaz de aumentar o poder explicativo do modelo baseado exclusivamente na turbidez, sugerindo que a relação entre turbidez e concentração de SST é variável sazonalmente. Mediante a comparação com balanços de massa, foram identificados alguns fatores que afetam o poder de predição da fórmula empírica desenvolvida pela American Water Works Association, algumas vezes de maneira drástica. Em geral, conclui-se que o uso de fórmulas empíricas principalmente em conjunto com modelos de regressão entre concentração de SST e turbidez possa não ser recomendável. / Most of the water treatment plant (WTP) residuals generated in Brazil is still discharged in water bodies, or disposed of in landfills. However, especially in large urban areas, ever stringent conditions for environmental permits e rising logistical costs have put into focus beneficial uses for those residuals. A major obstacle for paradigm change in that aspect lies in the fact that very rarely water treatment plant operators and designers are able to predict with some degree of certainty the mass and volume of residuals produced by the treatment process. Usually, empirical formulas are used for that end, which relates the residuals production rate to the concentration of total suspended solids (TSS) in the raw water, and the chemicals dose. The objectives of this work are: to compare the performance of two of the main quantitative estimation methods for residuals production the empirical formulas and the mass balance; to investigate the widespread practice of estimating the concentration of TSS using turbidity as a surrogate; and to identify the conditions under which such procedure is acceptable. For that end, data from six WTPs operated by SABESP (ABV, Alto Cotia, Cubatão, Guaraú, Franca e Presidente Prudente), plus 130 surface water monitoring stations operated by CETESB, was analyzed. Alternative regression models, employing other independent variables (color, average monthly flow and month) singly or in combination with turbidity, were developed. Only the inclusion of the month as a categorical variable was capable of enhancing the explaining power of the turbidity model, suggesting that the relation between turbidity and TSS concentration is seasonally variable. The results suggest that identification of such significant correlations between TSS concentration and turbidity is elusive at best, and doesn\'t amount to a trivial task. Out of the universe of 130 monitoring stations, in only 7 a good degree of correlation was found; of the WTPs, that was the case only in Presidente Prudente. Through the comparison with the mass balances, some factors that affect the predictive power of the American Water Works Association sometimes drastically a were identified. In general, it is concluded that the use of empirical formulas especially when combined with turbidity and TSS concentration regression models may not be recommended.

Grande parte do lodo gerado em ETAs no Brasil ainda é disposta em rios ou em aterros sanitários. Contudo, principalmente em grandes centros urbanos, condições de licenciamento ambiental restritivas e custos logísticos crescentes tem levantado interesse em usos benéficos para esse resíduo. Um obstáculo para a mudança de paradigma recai no fato de que muito raramente operadores e projetistas de ETAs nacionais conseguirem prever, com algum grau de confiabilidade, a massa e volume de resíduos produzidos pelo tratamento da água bruta. Geralmente, usa-se para esse fim fórmulas empíricas, que relacionam a produção de lodo à concentração de sólidos em suspensão totais (SST) na água bruta e à dosagem de produtos químicos. Os objetivos deste trabalho são: comparar o desempenho de dois dos principais métodos quantitativos de estimativa de produção de lodo o método de fórmulas empíricas, e o do balanço de massa; investigar a prática disseminada de se estimar a concentração de sólidos em suspensão totais na água bruta por meio de modelos de regressão linear com a turbidez como variável independente; e delinear condições para a aplicação dessa correlação. Foram utilizados dados de seis ETAs de ciclo completo operadas pela SABESP (ABV, Alto Cotia, Cubatão, Guaraú, Franca e Presidente Prudente), além de dados de monitoramento de 130 estações de monitoramento de águas superficiais da CETESB. Os resultados sugerem que a identificação de correlações significativas entre concentração de SST e turbidez é elusiva, e não constitui tarefa trivial. Do universo de 130 estações da CETESB, somente 7 apresentaram correlação significativa; das ETAs, somente Presidente Prudente. Modelos de regressão alternativos utilizando outras variáveis (cor, vazão média mensal e mês), combinadas com a turbidez ou isoladamente, foram desenvolvidos. Somente a inclusão do mês como variável categórica foi capaz de aumentar o poder explicativo do modelo baseado exclusivamente na turbidez, sugerindo que a relação entre turbidez e concentração de SST é variável sazonalmente. Mediante a comparação com balanços de massa, foram identificados alguns fatores que afetam o poder de predição da fórmula empírica desenvolvida pela American Water Works Association, algumas vezes de maneira drástica. Em geral, conclui-se que o uso de fórmulas empíricas principalmente em conjunto com modelos de regressão entre concentração de SST e turbidez possa não ser recomendável. / Most of the water treatment plant (WTP) residuals generated in Brazil is still discharged in water bodies, or disposed of in landfills. However, especially in large urban areas, ever stringent conditions for environmental permits e rising logistical costs have put into focus beneficial uses for those residuals. A major obstacle for paradigm change in that aspect lies in the fact that very rarely water treatment plant operators and designers are able to predict with some degree of certainty the mass and volume of residuals produced by the treatment process. Usually, empirical formulas are used for that end, which relates the residuals production rate to the concentration of total suspended solids (TSS) in the raw water, and the chemicals dose. The objectives of this work are: to compare the performance of two of the main quantitative estimation methods for residuals production the empirical formulas and the mass balance; to investigate the widespread practice of estimating the concentration of TSS using turbidity as a surrogate; and to identify the conditions under which such procedure is acceptable. For that end, data from six WTPs operated by SABESP (ABV, Alto Cotia, Cubatão, Guaraú, Franca e Presidente Prudente), plus 130 surface water monitoring stations operated by CETESB, was analyzed. Alternative regression models, employing other independent variables (color, average monthly flow and month) singly or in combination with turbidity, were developed. Only the inclusion of the month as a categorical variable was capable of enhancing the explaining power of the turbidity model, suggesting that the relation between turbidity and TSS concentration is seasonally variable. The results suggest that identification of such significant correlations between TSS concentration and turbidity is elusive at best, and doesn\'t amount to a trivial task. Out of the universe of 130 monitoring stations, in only 7 a good degree of correlation was found; of the WTPs, that was the case only in Presidente Prudente. Through the comparison with the mass balances, some factors that affect the predictive power of the American Water Works Association sometimes drastically a were identified. In general, it is concluded that the use of empirical formulas especially when combined with turbidity and TSS concentration regression models may not be recommended.

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No. of bitstreams: 3 Dissertação - Susane Campos Mota Angelim - 2015 (1).pdf: 18841997 bytes, checksum: 81d8b3c8746995f8815dfec4fc05909b (MD5) Dissertação - Susane Campos Mota Angelim - 2015 (2).pdf: 3115044 bytes, checksum: fb522cec32010b346517744c51a7c7c7 (MD5) license_rdf: 23148 bytes, checksum: 9da0b6dfac957114c6a7714714b86306 (MD5) Previous issue date: 2015-04-29 / Fundação de Amparo à Pesquisa do Estado de Goiás - FAPEG / In Brazil water treatment plants (WTP) residuals are usually discharged into waterways, with negative impacts on water quality, aquatic biota and sediments, which may also pose risks to human health. This paper presents a study on real scale disposal of aluminum sludge from the settling of a WTP in a primary facultative pond, both located in Piracanjuba-GO, wishing to contribute as an alternative for residuals management. The study aimed to evaluate the effects of WTP residuals (WTPR) in the performance of the wastewater stabilization pond (WSP), in terms of quality of the effluent and volume of bottom sludge accumulated. Worked up in two identical parallel ponds, one in which WTPR was applied (test pond) and another without application (control pond) to serve as comparison of results. The study was carried out in two stages, with dosage of 37 mg TS/L in Phase 1 and 44 mg TS/L in Phase 2, totaling 125 days of application and 191 days of monitoring. It was evaluated several effluent parameters such as BOD, solids, nitrogen, total phosphorus, Escherichia coli, metals, among others. Sludge volumes in the ponds were obtained from bathymetric survey using a sludge depth meter (sludge gun) and modeling by Surfer 8.0 software. The addition of the WTPR did not impair the performance of the test pond, with minimal reduction of BOD and nitrogen. It was not possible to identify any influence of WTPR for the removal of total phosphorus of the sewage, which was attributed to high pH and low dosage. There was no statistical difference (95% confidence level) between the means of 15 parameters evaluated in two phases, except for nitrogen ammonia. There was no difference between the increases of sludge volume accumulated in the bottom of the ponds, although total solids content was higher in the test pond. This behavior was associated with particle size characteristics of the material. The study indicates technical feasibility of WTP residuals disposal in the WSP studied, revealing an alternative for its management that can also be applied in other same type systems if evaluated the specific conditions in each case. / A realidade brasileira atual é de que a grande maioria dos resíduos de ETA são lançados diretamente em cursos d'água, com impactos negativos sobre a qualidade das águas, biota aquática e sedimentos, podendo também representar riscos à saúde humana. O trabalho apresenta um estudo em escala real da disposição do resíduo do decantador da ETA do tipo convencional (ou de ciclo completo) da cidade de Piracanjuba-GO, cujo coagulante utilizado é o sulfato de alumínio, na lagoa facultativa primária da ETE Piracanjuba, visando contribuir como alternativa adequada para a gestão dos resíduos sólidos de sistemas de saneamento. O trabalho teve como objetivo avaliar os efeitos da disposição do resíduo no desempenho da lagoa quanto à qualidade do efluente líquido e ao volume do lodo de fundo acumulado. Trabalhou-se com duas lagoas idênticas em paralelo, uma de teste, onde foi aplicado o resíduo, e outra de referência, sem aplicação, para servir de comparação dos resultados. O estudo foi realizado em duas fases de aplicação do resíduo e monitoramento das lagoas, com dosagem de 37 mgSTresíduo (bs)/Lesgoto na Fase 1 e 44 mgSTresíduo (bs)/Lesgoto na Fase 2, totalizando 125 dias de aplicação e 191 dias de monitoramento. Foram avaliados diversos parâmetros físico-químicos do efluente, tais como DBO, SST, Namoniacal, fósforo total, E.coli, metais, dentre outros. Os volumes de lodo nas lagoas foram obtidos a partir de levantamento batimétrico com uso de medidor de óptico de lodo (Sludge Gun) e calculados por modelagem matemática pelo programa Surfer 8.0. A adição do resíduo de ETA não prejudicou o desempenho da lagoa facultativa de teste, com discreta redução de DBO e Namoniacal. Não foi possível apontar nenhuma influência do resíduo de ETA sobre a remoção de fósforo total do esgoto, o que foi atribuído a fatores como elevado pH e baixa dosagem. Na análise estatística dos resultados do efluente, ao nível de confiança de 95%, não foram verificadas diferenças estatísticas entre as médias dos 15 parâmetros avaliados nas duas fases, exceto para Namoniacal. Não houve diferença entre os acréscimos de volume de lodo de fundo acumulado nas lagoas, sendo que concentração de sólidos totais do lodo de fundo foi maior na lagoa de teste. Esse comportamento foi associado a características granulométricas do material. O estudo indica a viabilidade técnica da disposição do resíduo da ETA nas lagoas facultativas da ETE Piracanjuba, mostrando-se como uma alternativa ambientalmente adequada para a gestão do resíduo, que pode ser aplicada também em outros sistemas de mesmas tipologias, desde que avaliadas as condições específicas de cada caso.

Orientador: Ricardo de Lima Isaac / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Civil e Arquitetura / Made available in DSpace on 2018-08-12T00:26:25Z (GMT). No. of bitstreams: 1 Ribeiro_CristianFonseca_M.pdf: 4603338 bytes, checksum: a0aa88f1b11066e7f0cd58dc278ad5f9 (MD5) Previous issue date: 2008 / Resumo: O presente trabalho aborda a utilização de um Sistema de Informações Geográficas (SIG) - recurso hoje indispensável para a análise de dados espacializados, amplamente utilizada no auxílio à tomada de decisão em diversos campos - como ferramenta de gestão do lodo gerado em Estações de Tratamento de Água (ETA) localizadas em uma mesma bacia hidrográfica. Esta gestão, em geral, é baseada em dados convencionais, ficando a mesma condicionada a informações estáticas. Os custos logísticos de transporte e disposição final em aterro sanitário, na maioria dos casos, são preponderantes em relação aos custos operacionais do sistema de tratamento do lodo. Diversos usos benéficos têm sido propostos por vários pesquisadores como melhor forma de destinação, do ponto de vista da sustentabilidade ambiental e econômica. Nesse caso, o material é considerado não mais como resíduo, mas como matéria-prima. O uso de informações espacializadas objetiva nesse caso facilitar a busca e seleção da alternativa mais adequada, tendo a localização geográfica dos potenciais usuários como critério diferencial em relação aos demais aspectos envolvidos na decisão. A área de estudo foi a das bacias hidrográficas dos rios Piracicaba, Capivari e Jundiaí (BH-PCJ). Diversos cenários foram gerados e avaliados. O gestor considerado foi ora uma determinada companhia de saneamento, ora um consórcio de todas as companhias de saneamento presentes na área ou um agrupamento delas. Para fins demonstrativos, as indústrias cerâmicas - para as quais a viabilidade técnico-econômica e ambiental já foi cientificamente comprovada - foram comparadas como destinação alternativa à disposição nos aterros licenciados existentes nessas bacias. Demonstrou-se, assim, o enorme potencial do SIG para a resolução de problemas de planejamento e gerenciamento de resíduos de ETA, tarefa essa que tende a se tornar cada vez mais difícil e complexa no contexto de uma bacia hidrográfica apresentando inúmeros geradores destes e de outros tipos de resíduos sólidos - tais como os resíduos urbanos, de estações de tratamento de esgoto, industriais - que competirão entre si sob as regras de livre mercado pelos já escassos e limitados aterros sanitários e também pelos diversos usuários dessa matéria-prima. / Abstract: Present work investigates the use of geographic information system (GIS) - nowadays a necessary technique for spatial data analysis, broadly used as decision-making aid in many fields - as a tool for watershed management for disposal or beneficial use of water treatment plants (WTP) sludge. Most of times, residuals management is based in conventional data, conditioned to stationary information. Logistic costs for transportation and landfill disposal, usually overcome sludge treatment system operating costs. Several beneficial uses have been proposed for many researchers as better solution rather than landfilling in terms of environmental and economical sustainability. This way, it is considered as raw material rather than residual. GIS appliance aims ease the search for best available alternative, having potential users geographic location as main criteria among other aspects involved in decision process. The territory studied was that of Rivers Piracicaba, Capivari and Jundiaí watershed, in southeastern region of Brazil. Several scenarios were generated and evaluated. The manager here was either a single water company, the consortium of all water companies or a small group of them. For demonstration purpose, ceramic brick plants - whose technical, economical and environmental sustainability was previously demonstrated - were compared to sanitary landfill as final disposal. GIS high potential for WTP sludges planning and management, task that trends to become more and more difficult and complex in a context of a watershed containing several generators of these and other kinds of solid wastes - as municipal wastes, wastewater treatment plant sludge, industrial wastes - that struggle each other under free market rules for scarce and limited sanitary landfills and also for every users of these materials - was demonstrated. / Mestrado / Saneamento e Ambiente / Mestre em Engenharia Civil

The provision of clean drinking water typically involves treatment processes to remove contaminants. The conventional process involves coagulation with hydrolysing metal salts, typically of aluminium (‘alum’) or trivalent iron (‘ferric’). Along with the product water this also produces a waste by-product, or sludge. The fact of increasing sludge production — due to higher levels of treatment and greater volume of water supply — conflicts with modern demands for environmental best practice, leading to higher financial costs. A further issue is the significant quantity of water that is held up in the sludge, and wasted. / One means of dealing with these problems is to dewater the sludge further. This reduces the volume of waste to be disposed of. The consistency is also improved (e.g. for the purpose of landfilling). And a significant amount of water can be recovered. The efficiency, and efficacy, of this process depends on the dewaterability of the sludge.In fact, good dewaterability is vital to the operation of conventional drinking water treatment plants (WTP’s). The usual process of separating the particulates, formed from a blend of contaminants and coagulated precipitate, relies on ‘clarification’ and ‘thickening’, which are essentially settling operations of solid–liquid separation.WTP operators — and researchers — do attempt to measure sludge dewaterability, but usually rely on empirical characterisation techniques that do not tell the full story and can even mislead. Understanding of the physical and chemical nature of the sludge is also surprisingly rudimentary, considering the long history of these processes. / The present work begins by reviewing the current state of knowledge on raw water and sludge composition, with special focus on solid aluminium and iron phases and on fractal aggregate structure. Next the theory of dewatering is examined, with the adopted phenomenological theory contrasted with empirical techniques and other theories.The foundation for subsequent analyses is laid by experimental work which establishes the solid phase density of WTP sludges. Additionally, alum sludges are found to contain pseudoböhmite, while 2-line ferrihydrite and goethite are identified in ferric sludges. / A key hypothesis is that dewaterability is partly determined by the treatment conditions. To investigate this, numerous WTP sludges were studied that had been generated under diverse conditions: some plant samples were obtained, and the remainder were generated in the laboratory (results were consistent). Dewaterability was characterised for each sludge in concentration ranges relevant to settling, centrifugation and filtration using models developed by LANDMAN and WHITE inter alia; it is expressed in terms of both equilibrium and kinetic parameters, py(φ) and R(φ) respectively.This work confirmed that dewaterability is significantly influenced by treatment conditions.The strongest correlations were observed when varying coagulation pH and coagulant dose. At high doses precipitated coagulant controls the sludge behaviour, and dewaterability is poor. Dewaterability deteriorates as pH is increased for high-dose alum sludges; other sludges are less sensitive to pH. These findings can be linked to the faster coagulation dynamics prevailing at high coagulant and alkali dose.Alum and ferric sludges in general had comparable dewaterabilities, and the characteristics of a magnesium sludge were similar too.Small effects on dewaterability were observed in response to variations in raw water organic content and shearing. Polymer flocculation and conditioning appeared mainly to affect dewaterability at low sludge concentrations. Ageing did not produce clear changes in dewaterability.Dense, compact particles are known to dewater better than ‘fluffy’ aggregates or flocs usually encountered in drinking water treatment. This explains the superior dewaterability of a sludge containing powdered activated carbon (PAC). Even greater improvements were observed following a cycle of sludge freezing and thawing for a wide range of WTP sludges. / Further aspects considered in the present work include deviations from simplifying assumptions that are usually made. Specifically: investigation of long-time dewatering behaviour, wall effects, non-isotropic stresses, and reversibility of dewatering (or ‘elasticity’).Several other results and conclusions, of both theoretical and experimental nature, are presented on topics of subsidiary or peripheral interest that are nonetheless important for establishing a reliable basis for research in this area. / This work has proposed links between industrial drinking water coagulation conditions, sludge dewaterability from settling to filtration, and the microstructure of the aggregates making up that sludge. This information can be used when considering the operation or design of a WTP in order to optimise sludge dewaterability, within the constraints of producing drinking water of acceptable quality.