From the Proceedings of the 1971 Meetings of the Arizona Section - American Water Resources Assn. and the Hydrology Section - Arizona Academy of Science - April 22-23, 1971, Tempe, Arizona / Sewage effluent is commonly used for the irrigation of crops that are not consumed raw. Due to continued population growth in the Salt River Valley, Arizona, economic reuse of municipal waste waters is becoming essential. The salt river bed has about 3 ft of fine loamy sand underlain by sand and gravel layers to great depth and a groundwater table at about 10 ft depth. These conditions are very favorable for high-rate waste water reclamation by groundwater recharge. The activated sludge plant in phoenix will probably be discharging 250 mgd by the year 2000. At 4.5 ft average annual water use, this could irrigate about 70,000 acres, possibly more than agriculture will need at that time. A sewage effluent renovation pilot project was located about 1.5 miles from the plant. It contains 6 parallel recharge basins 20 to 700 ft each, spaced 20 ft apart. The basins were covered by grass, gravel or were left bare. Observation wells were installed at various locations in the area. Results indicated that infiltration rates were fastest in the grassy basins. Phosphate, nitrogen and median fecal coliform levels were all lower after this form of tertiary treatment. Practical details of the application of this water reclamation method in the Salt River Valley are outlined. Costs would be 5 dollars/af, less than 1/10 the equivalent costs of in-plant tertiary treatments.

From the Proceedings of the 1974 Meetings of the Arizona Section - American Water Resources Assn. and the Hydrology Section - Arizona Academy of Science - April 19-20, 1974, Flagstaff, Arizona / The process of salt replacement desalination proposed is believed to be able to produce vast quantities of fresh water be desalination. This method, which is a novel approach to minimizing the costs of saline water conversion, consists of the substitution of solutes in a solution to be desalted by a replacer chemical, and the low energy removal of that replacer chemical. The ultrafiltration of larger molecular sized replacer chemicals with high flux membranes increases the produce yield rate and reduces the corresponding energy requirement, with respect to reverse osmosis. In addition, the initial captial investment is less since no pressure constraining devices are required. The alteration of the osmotic pressure of the replacer solution within the process can also take advantage of energy savings through the utilization of an easily reversible reaction which synthesizes and breaks down a constituent that has a significant osmotic pressure difference between phases. Finally, the unusual process of fixed gel syneresis shows potential as a low energy salt replacement type process, but still requires extensive investigation.

The Ceratium species occurring in the Vaal River since 2000, was identified as Ceratium hirundinella (O.F. Müller) Dujardin as proposed by Van Ginkel et al (2001). Ceratium hirundinella is known to cause problems in drinking water purification and has been penetrating into the final drinking water of Rand Water since 2006. Ceratium hirundinella is associated with many other water purification problems such as disrupting of the coagulation and flocculation processes, blocking of sand filters and algal penetration into the drinking water. Ceratium hirundinella also produce fishy taste and odorous compounds and causes discolouration of the water. The aims of this study were to determine the main environmental factors which are associated with the bloom formation of C. hirundinella in the source water and to investigate the influence of C. hirundinella on the production of potable water. In order to optimise treatment processes and resolve problems associated with high C. hirundinella concentrations during the production of potable water, jar testing and chlorine exposure experiments were performed. Multivariate statistical analyses were performed to determine the main environmental variables behind C. hirundinella blooms. Ten years data (2000 - 2009) from the sampling point C–VRB5T in the Vaal River, (5 km upstream from the Barrage weir) were used for this investigation, because C. hirundinella occurred there frequently during the ten year period. In this study, it was found that C. hirundinella was favoured by high pH, Chemical Oxygen Demand (COD), orthophoshapte (PO4), and silica concentrations, as well as low turbidity and low dissolved inorganic nitrogen (DIN) concentrations. No correlation was found between C. hirundinella and temperature, suggesting that this alga does not occur during periods of extreme warm or extreme cold conditions, but most probably during autumn and spring. The results of the multivariate statistical analysis performed with historical data from Vaalkop dam, indicate that the dinoflagellate C. hirundinella seems to be favoured by low temperature and turbidity, and high DIN, Fe, Methyl–orange alkalinity, Cd, PO4, Conductivity, pH, hardness and SO4 concentrations. In order to optimise treatment processes such as coagulation, flocculation and sedimentation, jar testing experiments were performed to investigate different coagulant chemicals namely: cationic poly–electrolyte only, cationic poly–electrolyte in combination with slaked lime (CaO) and CaO in combination with activated silica. Water from four different sampling localities were chosen to perform the different jar testing experiments: 1) sampling point M–FOREBAY (in the Forebay, connecting the canal to the Zuikerbosch Purification plant) near Vereeniging due to its proximity to the Zuikerbosch treatment plant, 2) M–CANAL_VD (upstream from the inflow of the recovered water from Panfontein) to determine the influence of (if any) the recovered water from Panfontein on Forebay source water, 3) source water from Vaalkop Dam (M–RAW_VAALKOP) and 4) source water from Rietvlei Dam (water from both Vaalkop and Rietvlei Dams contained high concentrations of C. hirundinella at that time of sampling) to determine which coagulant chemical is the most effective in removing high concentrations of C. hirundinella cells during the production of drinking water. The jar testing experiments with Vaalkop Dam and Rietvlei Dam source water (rich with C. hirundinella) indicated that using cationic poly–electrolyte alone did not remove high concentrations of C. hirundinella efficiently. However, when CaO (in combination with cationic poly–electrolyte or activated silica) were dosed to Vaalkop Dam source water a significant decrease of C. hirundinella concentration was observed. This indicates that the C. hirundinella cells were “shocked or stressed” when exposed to the high pH of the CaO, rendering it immobile and thereby enhancing the coagulation and flocculation process. However, when 10 mg/L CaO in combination with poly–electrolyte was dosed to Rietvlei Dam source water the turbidity and chlorophyll–665 results indicated that this coagulant chemical procedure was ineffective in removing algal material from the source water. The jar testing experiments using the cationic poly–electrolyte alone or cationic poly–electrolyte in combination with CaO on M–FOREBAY and M–CANAL_VD source water, showed a decrease in turbidity, chlorophyll–665 concentration, and total algal biomass, with an increase of coagulant chemical. When CaO in combination with activated silica was dosed, the inherent turbidity of the lime increased the turbidity of the Vaalkop Dam, M–FOREBAY and M–CANAL_VD source water to such an extent that it affected coagulation negatively, resulting in high turbidity values in the supernatant. Regardless of the turbidity values, the chlorophyll–665 concentration and total algal biomass (C. hirundinella specifically in Vaalkop Dam source water) decreased significantly when CaO was dosed in combination with activated silica. Therefore it was concluded that a cationic poly–electrolyte alone is a good coagulant chemical for the removal of turbidity, but when high algal biomass occur in the source water it is essential to add CaO to “stress” or “shock” the algae for the effective removal thereof. However, when CaO in combination with activated silica was dosed to Rietvlei Dam source water a decrease in turbidity and chlorophyll–665 concentration was found with an increasing coagulant chemical concentration. These results confirm the fact that coagulant chemicals may perform differently during different periods of the year when water chemistry changes and that certain coagulant chemicals may never be suitable to use for certain source waters. For the effective removal of algae during water purification, it is recommended that cationic poly–electrolyte in combination with CaO are used as coagulant chemical at the Zuikerbosch Water Purification Plant. Turbidity is not a good indication of algal removal efficiency during jar testing experiments. If problems with high algal concentrations in the source water are experienced it is advisable to also determine the chlorophyll–665 concentrations of the supernatant water during the regular jar testing experiments, since it will give a better indication of algal removal. Chlorine exposure experiments were performed on water from Vaalkop Dam (M–RAW_VAALKOP) and Rietvlei Dam source water, to determine the possibility of implementing pre– or intermediate chlorination with the aim to render the cells immobile for more effective coagulation. The chlorine exposure experiments with Vaalkop Dam and Rietvlei Dam source water showed similar results. The chlorine concentration to be dosed as part of pre– or intermediate chlorination will differ for each type of source water as the chemical and biological composition of each water body are unique. When the effect of chlorine on the freshwater dinoflagellate C. hirundinella was investigated, it was found that the effective chlorine concentration where 50 % of Ceratium cells were rendered immobile (EC50) was approximately 1.16 mg/L for Vaalkop Dam source water. For the source water sampled from Rietvlei Dam, it was found that the EC50 was at approximately 0.87 mg/L. Results of analyses to determine the organic compounds in the water after chlorination revealed that an increase in chlorine concentration resulted in increase in total organic carbon concentration (TOC), as well as a slight increase in MIB and trihalomethanes (CHCl3). Pre– or intermediate chlorination seem to be an effective treatment option for the dinoflagellate C. hirundinella to be rendered immobile and thereby assisting in its coagulation process. The use of pre– or intermediate chlorination to effectively treat source waters containing high concentrations of C. hirundinella is a viable option to consider. However, the organic compounds in the water should be monitored and the EC50 value for each source water composition should be determined carefully as to restrict cell lysis and subsequent release of organic compounds into the water. / Thesis (M.Sc. (Environmental Science))--North-West University, Potchefstroom Campus, 2012.

The Ceratium species occurring in the Vaal River since 2000, was identified as Ceratium hirundinella (O.F. Müller) Dujardin as proposed by Van Ginkel et al (2001). Ceratium hirundinella is known to cause problems in drinking water purification and has been penetrating into the final drinking water of Rand Water since 2006. Ceratium hirundinella is associated with many other water purification problems such as disrupting of the coagulation and flocculation processes, blocking of sand filters and algal penetration into the drinking water. Ceratium hirundinella also produce fishy taste and odorous compounds and causes discolouration of the water. The aims of this study were to determine the main environmental factors which are associated with the bloom formation of C. hirundinella in the source water and to investigate the influence of C. hirundinella on the production of potable water. In order to optimise treatment processes and resolve problems associated with high C. hirundinella concentrations during the production of potable water, jar testing and chlorine exposure experiments were performed. Multivariate statistical analyses were performed to determine the main environmental variables behind C. hirundinella blooms. Ten years data (2000 - 2009) from the sampling point C–VRB5T in the Vaal River, (5 km upstream from the Barrage weir) were used for this investigation, because C. hirundinella occurred there frequently during the ten year period. In this study, it was found that C. hirundinella was favoured by high pH, Chemical Oxygen Demand (COD), orthophoshapte (PO4), and silica concentrations, as well as low turbidity and low dissolved inorganic nitrogen (DIN) concentrations. No correlation was found between C. hirundinella and temperature, suggesting that this alga does not occur during periods of extreme warm or extreme cold conditions, but most probably during autumn and spring. The results of the multivariate statistical analysis performed with historical data from Vaalkop dam, indicate that the dinoflagellate C. hirundinella seems to be favoured by low temperature and turbidity, and high DIN, Fe, Methyl–orange alkalinity, Cd, PO4, Conductivity, pH, hardness and SO4 concentrations. In order to optimise treatment processes such as coagulation, flocculation and sedimentation, jar testing experiments were performed to investigate different coagulant chemicals namely: cationic poly–electrolyte only, cationic poly–electrolyte in combination with slaked lime (CaO) and CaO in combination with activated silica. Water from four different sampling localities were chosen to perform the different jar testing experiments: 1) sampling point M–FOREBAY (in the Forebay, connecting the canal to the Zuikerbosch Purification plant) near Vereeniging due to its proximity to the Zuikerbosch treatment plant, 2) M–CANAL_VD (upstream from the inflow of the recovered water from Panfontein) to determine the influence of (if any) the recovered water from Panfontein on Forebay source water, 3) source water from Vaalkop Dam (M–RAW_VAALKOP) and 4) source water from Rietvlei Dam (water from both Vaalkop and Rietvlei Dams contained high concentrations of C. hirundinella at that time of sampling) to determine which coagulant chemical is the most effective in removing high concentrations of C. hirundinella cells during the production of drinking water. The jar testing experiments with Vaalkop Dam and Rietvlei Dam source water (rich with C. hirundinella) indicated that using cationic poly–electrolyte alone did not remove high concentrations of C. hirundinella efficiently. However, when CaO (in combination with cationic poly–electrolyte or activated silica) were dosed to Vaalkop Dam source water a significant decrease of C. hirundinella concentration was observed. This indicates that the C. hirundinella cells were “shocked or stressed” when exposed to the high pH of the CaO, rendering it immobile and thereby enhancing the coagulation and flocculation process. However, when 10 mg/L CaO in combination with poly–electrolyte was dosed to Rietvlei Dam source water the turbidity and chlorophyll–665 results indicated that this coagulant chemical procedure was ineffective in removing algal material from the source water. The jar testing experiments using the cationic poly–electrolyte alone or cationic poly–electrolyte in combination with CaO on M–FOREBAY and M–CANAL_VD source water, showed a decrease in turbidity, chlorophyll–665 concentration, and total algal biomass, with an increase of coagulant chemical. When CaO in combination with activated silica was dosed, the inherent turbidity of the lime increased the turbidity of the Vaalkop Dam, M–FOREBAY and M–CANAL_VD source water to such an extent that it affected coagulation negatively, resulting in high turbidity values in the supernatant. Regardless of the turbidity values, the chlorophyll–665 concentration and total algal biomass (C. hirundinella specifically in Vaalkop Dam source water) decreased significantly when CaO was dosed in combination with activated silica. Therefore it was concluded that a cationic poly–electrolyte alone is a good coagulant chemical for the removal of turbidity, but when high algal biomass occur in the source water it is essential to add CaO to “stress” or “shock” the algae for the effective removal thereof. However, when CaO in combination with activated silica was dosed to Rietvlei Dam source water a decrease in turbidity and chlorophyll–665 concentration was found with an increasing coagulant chemical concentration. These results confirm the fact that coagulant chemicals may perform differently during different periods of the year when water chemistry changes and that certain coagulant chemicals may never be suitable to use for certain source waters. For the effective removal of algae during water purification, it is recommended that cationic poly–electrolyte in combination with CaO are used as coagulant chemical at the Zuikerbosch Water Purification Plant. Turbidity is not a good indication of algal removal efficiency during jar testing experiments. If problems with high algal concentrations in the source water are experienced it is advisable to also determine the chlorophyll–665 concentrations of the supernatant water during the regular jar testing experiments, since it will give a better indication of algal removal. Chlorine exposure experiments were performed on water from Vaalkop Dam (M–RAW_VAALKOP) and Rietvlei Dam source water, to determine the possibility of implementing pre– or intermediate chlorination with the aim to render the cells immobile for more effective coagulation. The chlorine exposure experiments with Vaalkop Dam and Rietvlei Dam source water showed similar results. The chlorine concentration to be dosed as part of pre– or intermediate chlorination will differ for each type of source water as the chemical and biological composition of each water body are unique. When the effect of chlorine on the freshwater dinoflagellate C. hirundinella was investigated, it was found that the effective chlorine concentration where 50 % of Ceratium cells were rendered immobile (EC50) was approximately 1.16 mg/L for Vaalkop Dam source water. For the source water sampled from Rietvlei Dam, it was found that the EC50 was at approximately 0.87 mg/L. Results of analyses to determine the organic compounds in the water after chlorination revealed that an increase in chlorine concentration resulted in increase in total organic carbon concentration (TOC), as well as a slight increase in MIB and trihalomethanes (CHCl3). Pre– or intermediate chlorination seem to be an effective treatment option for the dinoflagellate C. hirundinella to be rendered immobile and thereby assisting in its coagulation process. The use of pre– or intermediate chlorination to effectively treat source waters containing high concentrations of C. hirundinella is a viable option to consider. However, the organic compounds in the water should be monitored and the EC50 value for each source water composition should be determined carefully as to restrict cell lysis and subsequent release of organic compounds into the water. / Thesis (M.Sc. (Environmental Science))--North-West University, Potchefstroom Campus, 2012.

Inadequately treated wastewater effluent is harmful to the receiving aquatic environment. Water-borne chemicals and microbial pathogens pose a health risk to anyone living downstream from sewage treatment facilities. This study assessed the effluent from a package plant with a design capacity of 48kℓ/24 hours, servicing 12 household units and a restaurant in Mogale City. Over a 12 month period, fortnightly water samples were collected from ten selected sites including two boreholes, a river and two dams. Standard parameters including physical (pH, EC, temperature, DO and SS), chemical (nutrient concentration) and biological (bacterial counts) were analysed using handheld meters, standard membrane filter techniques and colorimetric methods. One borehole was affected by pathogen and nitrate runoff from an adjacent poultry farm. If regularly monitored, the package plant effectively removed microbes (most samples contained 0 cfu/100mℓ) but above limit COD, ammonia and phosphate was released in the effluent (with maximum values of 322 mg/ℓ, 42.52 mg/ℓ and 7.18 mg/ℓ, respectively). Generally, river and dam water at the site was of good quality. / Environmental Science / M. Sc. (Environmental Science)

Coal seams are commonly associated with poor quality water that requires treatment. Water treatment can be very expensive and can severely affect the profitability of mining projects. This study investigated the potential cultivation of Arthrospira maxima (Spirulina) in coal seam water to beneficiate coal seam water in order to effectively offset the water treatment cost. The study was conducted in Northern South Africa and formed part of a larger Coal Seam Water Beneficiation Project (CSWBP). The study consisted of laboratory based Flask Studies and outdoor High Rate Algal Pond Studies. The Flask Studies that were carried out in the on-site field laboratory, found that the coal seam water could provide a suitable medium for Spirulina cultivation. In addition, it was found that the optimal pH for the selected strain ranged between 9 - 10.5 and that the addition of excess iron, up to 100 times the concentration found in defined growth media such as Schlösser’s, to the culture media could enhance productivity. The High Rate Algal Pond Studies (HRAP) were carried out over a period of 18 months. The studies showed that the coal seam water at the CSWBP is a valuable resource that can reduce media costs by 50% without affecting productivity. In a study encompassing 334 days it was shown that heating the culture through plate heat exchangers would result in a significant increase in productivity and a heated productivity of 19.86 g/m2/day was recorded. An unheated productivity of 14.11 g/m2/day was recorded. Therefore, it was found that it would be economically feasible to beneficiate coal seam water found at the CSWBP through the cultivation of Arthrospira maxima (Spirulina). / Environmental Sciences / M. Sc. (Environmental Science)

A presença de fármacos em águas superficiais, subterrâneas, solo e efluentes tem gerado preocupações no que diz respeito à ineficiência dos tratamentos convencionais e os riscos ambientais associados ao descarte inadequado destes micropoluentes emergentes. Diante disto, o objetivo deste trabalho foi avaliar a adsorção e a dessorção de ácido acetilsalicílico (AAS) em solução aquosa em carvão ativado de babaçu in natura (CAB) e funcionalizado quimicamente com HNO3 (CAA). Foram determinados aos adsorventes os teores de cinzas, umidade e de material volátil, granulometria, análise elementar, aspectos morfológicos dos adsorventes, por meio de microscopia eletrônica de varredura (MEV), pH no ponto de carga zero (pHPCZ), características da superfície dos adsorventes por meio de adsorção/dessorção de N2 e os grupos funcionais por espectroscopia na região no infravermelho (FTIR) e método de Boehm. Ensaios cinéticos, de equilíbrio e termodinâmicos foram conduzidos para a adsorção e dessorção em batelada. Ensaios em coluna de leito fixo foram conduzidos preliminarmente. Os resultados dos ensaios cinéticos de adsorção e dessorção foram ajustados aos modelos de pseudo-primeira e pseudo-segunda ordem e os resultados de equilíbrio de adsorção aos modelos matemáticos de Langmuir e Freundlich e de dessorção ao modelo de Langmuir-Freundlich. Aos resultados termodinâmicos de adsorção e dessorção foram determinados os valores de ΔG º, ΔH º e ΔS º. Os adsorventes apresentaram características microporosas, com valores de pHPCZ de 6,4 para CAB e 4,5 para CAA que interferem diretamente na adsorção. Os dados da cinética de adsorção foram melhor ajustados ao modelo de pseudo-segunda ordem e os do equilíbrio de adsorção ao modelo de Langmuir. Os resultados do ΔG º e ΔH º resultaram negativos e o do ΔSº positivo nas temperaturas de 25 ºC, 45 ºC e 55 ºC, indicando que o processo é exotérmico e espontâneo. O aumento da temperatura favoreceu a adsorção com o CAB, e reduziu a capacidade adsortiva do CAA. Em pH ácido a quantidade máxima adsorvida do AAS foi de 119,80 mg g -1 para CAB e 115,08 mg g -1 para CAA. Nos ensaios de dessorção os melhores resultados foram observados com o CAB em pHPCZ = 6,4. Os resultados cinéticos tiveram melhor ajuste ao modelo de pseudo-primeira ordem. As isotermas de dessorção ajustadas ao modelo de Langmuir-Freundlich. Adicionalmente, com os ciclos foram obtidos os percentuais médios de adsorção e dessorção de 92% e 75% no CAB e de 72% e 10% no CAA, respectivamente. O conjunto de dados de pH e temperatura avaliados nos ensaios em coluna de leito fixo determinaram que a reação de adsorção é melhor definida em pH 2,0 e temperatura de 40 ºC. / The presence of drugs in surface water, groundwater, soil and effluents has raised concerns regarding the inefficiency of conventional treatments and the environmental risks associated with the inappropriate disposal of these emerging micropollutants. The objective of this work was to evaluate the adsorption and desorption of acetylsalicylic acid (AAS) in aqueous solution of in natura activated babassu carbon (CAB) and chemically functionalized with HNO3 (CAA). The ash adsorbents, moisture and volatile matter, granulometry, elemental analysis, morphological aspects of the adsorbents were determined by scanning electron microscopy (SEM), pH at the zero load point (pHPCZ), surface characteristics of the adsorbents. adsorbents by adsorption/desorption of N2 and functional groups by infrared spectroscopy (FTIR) and Boehm method. Kinetic, equilibrium and thermodynamic tests were conducted for batch adsorption and desorption. Preliminary tests were conducted in a fixed bed column. The adsorption and desorption kinetics results were adjusted to the pseudofirst and pseudo-second order models and the adsorption equilibrium results to the Langmuir and Freundlich mathematical models. The values of ΔG º, ΔH º and ΔS º were determined for the thermodynamic adsorption and desorption results. The desorption equilibrium results were fitted to the Langmuir-Freundlich model. The adsorbents presented microporous characteristics, with values of pHPCZ of 6.4 for CAB and 4,5 for CAA that interfere directly in the adsorption. Adsorption was favored at acidic pH in both adsorbents. The adsorption kinetics data were better fitted to the pseudo second order model and those of the adsorption equilibrium to the Langmuir model, indicating the influence of the chemisorption on the adsorption. The results of ΔGº and ΔHº were negative and that of ΔSº positive at temperatures of 25 ºC, 45 ºC and 55 ºC, indicating the influence of the chemisorption in the process that is exothermic and spontaneous. The increase in temperature favored the adsorption with the CAB, and reduced the adsorptive capacity of the CAA. At acid pH the maximum adsorbed amount of ASA was 119.80 mg g -1 for CAB and 115.08 mg g -1 for CAA. In the desorption experiments the best results were observed with the CAB at pHPCZ = 6.4. The kinetic results had better fit to the pseudo first order model. Desorption isotherms fitted to the Langmuir-Freundlich model indicated affinity between the CAB, ASA and the chosen regenerant. Additionally, the average adsorption and desorption percentages of 92% and 75% in CAB and 72% and 10% in CAA, respectively, were obtained with the cycles. The set of pH and temperature data evaluated in the fixed bed column assays determined that the adsorption reaction is best defined at pH 2.0 and temperature of 40 ºC.

Thesis submitted in the requirements for the degree Doctor Technologiae: Chemical Engineering in the Faculty of Engineering at the CAPE PENINSULA UNIVERSITY OF TECHNOLOGY, 2013 / To date, limited information has been published on textile wastewater treatment, for re-use, in South Africa (SA), with treatment processes focusing on conventional wastewater treatment methods. A large contributor to the contamination of water within textile industries is from dyehouse processes. A major concern in textile wastewater treatment is the release of azo dyes and their metabolites, some of which are carcinogenic and mutanogenic, into the environment since they are xenobiotic and aerobically recalcitrant to biodegradation. A necessity therefore exists to find an effective treatment method capable of removing both the strong colour and the toxic organic compounds from textile wastewater. Membrane bioreactors (MBRs) are favoured when treating high-strength wastewater, since the membrane area is determined by the hydraulic throughput and not the biological load; no sludge is wasted and all bacteria are retained within the reactor, including specific bacteria capable of degrading the toxic, non-biodegradable constituents present in textile wastewater. MBR systems, using various configurations have been utilised extensively in the rest of the world to treat textile wastewater at both lab and pilot-scale. This DTech project formed part of a collaborative Water Research Commission (WRC) funded project K5/1900 - Pilot application of a dual-stage membrane bioreactor (dsMBR) for industrial wastewater treatment. The main purpose of this study was the on-site evaluation of a pilot-scale dsMBR incorporating two ultrafiltration (UF) sidestream membrane modules for the treatment, recovery and re-use of textile wastewater. The objectives of this project were to determine the treatment efficiency of the system; to evaluate the degree of colour removal from the textile wastewater; to improve residual colour removal within the system using treatment processes, such as NF and RO, as well as to propose a design and cost for a full-scale plant. A textile industry located in Bellville, Western Cape, was chosen as the industrial partner for the on-site evaluation of a semi-automated pilot wastewater treatment MBR plant using two 5.1 m2 Norit X-flow AirliftTM membrane modules. Since the wastewater treatment system was located on the premises, real continuously changing industrial wastewater was being treated. The industrial textile wastewater was treated in a series of tanks: 1) an anaerobic tank, which cleaved the azo bonds of the reactive dyes; 2) an anoxic tank containing reduced amounts of dissolved oxygen, in which denitrification occurred; and 3) an aerobic tank, in which i) nitrification, as well as ii) mineralisation of the aromatic amines occurred. The UF-membrane modules would account for the removal of any organic material. The wastewater stream was characterised by a chemical oxygen demand (COD) range of between 45 to 2,820 mg/L and an average biological oxygen demand (BOD) of 192.5 mg/L. The dsMBR achieved an average COD reduction of 75% with a maximum of 97% over the 220 day test period. The COD concentration obtained after dsMBR treatment averaged at 191 mg/L, which was well within the City of Cape Town industrial wastewater discharge standard. The average reduction in turbidity and TSS was 94% and 19.6%, respectively, during the UF-MBR stage of the system. Subsequent treatment of the UF permeate with nanofiltration (NF) for 4 days, alternated with reverse osmosis (RO) for 14 days removed both the residual colour and salt present in the UF permeate. A consistent reduction in the colour of the incoming wastewater was evident. The colour in the wastewater was reduced from an average of 659 ADMI units to ~12 ADMI units in the NF permeate, a lower American dye manufacturing index (ADMI) (i.e. method of colour representation) compared to the potable water (~17 ADMI units) utilised by the industrial partner in their dyeing processes. The colour was reduced from an average of 659 to ~20 ADMI units in the RO permeate, a lower ADMI and therefore colour when compared to the potable water. An average conductivity rejection of 91% was achieved with conductivity being reduced from an average of 7,700 to 693 μS/cm and the TDS reduced from an average of 5,700 to 473 mg/L, which facilitated an average TDS rejection of 92%. Based on the composition of the UF permeate fed to the RO membrane a maximum removal of 98.7% was achieved for both conductivity and total dissolved solids (TDS). The proposed full-scale plant would incorporate a UF-MBR system, followed by NF, RO, flocculation and a filter press. Therefore, the two waste products produced during operation of the proposed full-scale plant, would be the solid filter cakes and the liquid filtrate from the filter press. Implementing the proposed full-scale plant it would cost the industrial partner an operating cost of ZAR 113.85 and ZAR 3,415.49 to treat 97.1 m3 and 2,913 m3 of textile wastewater, respectively, per day and per month. This results in an annual saving of ZAR 845,848 on potable water expenses. This research, would provide SA textile industries, with an option to: 1) reduce their water consumption, thereby utilising less of a valuable decreasing commodity; 2) meet the SA government discharge standards and reduce their discharge costs; 3) reduce their carbon footprint (i.e. reduce their impact on the environment) by re-using their treated wastewater and therefore using less water from the municipality; and 4) decrease their annual expenditure on water, since the treated wastewater would be available for re-use.

CAPES / A escassez, deterioração da qualidade dos mananciais e o aumento da demanda por água tem sido problema global. Diante desses problemas o uso de fontes alternativas é citado como solução, com destaque para o aproveitamento de água da chuva. Em alguns locais, a água da chuva escoada de telhados tem sido utilizada para fins potáveis e não potáveis e a água da chuva in natura tem qualidade superior ao de águas superficiais e subterrâneas. Embora a água da chuva tenha qualidade físico-química dentro dos padrões de potabilidade, é necessário melhorar sua qualidade para utilizá-la. Assim neste trabalho é avaliado o tratamento da água da chuva por filtro ascendente (volume de 35,4 L) com meio suporte de 0,50 m de seixo rolado e camada filtrante composta de 0,15m de brita, 0,25 m de areia e 0,55 m de carvão ativado e desinfecção por radiação UV. Para melhorar a qualidade da água antes de chegar ao filtro foi instalado um dispositivo de primeiro descarte com volume de 41,4 L. A avaliação do tratamento foi realizada através da análise dos parâmetros pH, temperatura, cor, oxigênio dissolvido, turbidez, amônia, nitrito, nitrato, fosfato, sulfato, DQO e coliformes. Os valores médios obtidos para os parâmetros físico-químicos da água após o tratamento foram de 6,7 para o pH, 22,3 °C para a temperatura, 12,5 UPC para cor, 6,7 mg/L para OD, 0,5 UNT para turbidez, 0,2 mg/L para amônia, 0,01 mg/L para nitrito, 1,7 mg/L para nitrato, 0,2 mg/L para fosfato, 0,7 mg/L para sulfato e 1,3 mg/L para DQO. O tratamento proposto obteve resultados de eficiência para remoção de cor de 22,4%, turbidez de 28,6%, amônia de 50,0%, nitrito de 23,1%, nitrato de 37,0%, fosfato de 95,1% sulfato de 41,7% e DQO de 66,7% e reduziu o numero de microrganismos para um valor menor que o limite detectável do método de análise. Todos os valores médios obtidos para os parâmetros físico-químicos atendem aos padrões exigidos pela portaria 2914/2011 do Ministério da Saúde para água potável. / The scarcity, quality deterioration of water sources and increasing demand for water has been global problem. Faced with these problems the use of alternative sources is cited as a solution, especially taking advantage of rainwater. In some places, rainwater drained roofs have been used for potable and non-potable purposes and rainwater in nature has superior quality to the surface water and groundwater. Although rainwater has physicochemical quality within the potability standards, it is necessary to improve their quality to use it. Thus this work is evaluated treatment of rainwater by upflow filter (35,4 L volume) with support means of 0,50 m of Boulder and filter layer of 0,15 m of crushed stone, 0,25 m of sand and 0,55 m of activated carbon and UV disinfection. To enhance the water quality before reaching the filter was installed a first-flush device with volume of 41,4 L. The characterization of the water before and after treatment was performed through analysis of parameters pH, temperature, color, dissolved oxygen, turbidity, ammonia, nitrite, nitrate, phosphate, sulphate, COD and coliforms. The mean values obtained for the physicochemical parameters of the water after treatment were 6,7 to pH 22,3 °C for temperature, 12,5 UPC for color, 6,7 mg/L to OD, 0,5 NTU for turbidity, 0,2mg/L for ammonia, 0,01 mg/L for nitrite, 1,7 mg/L for nitrate, 0,2 mg/L for phosphate,0,7 mg/L for sulfate and 1,3 mg/L for COD. The obtained results proposed treatment for color removal efficiency of 22,4%, haze 28,6%, 50,0% ammonia, 23,1% nitrite, nitrate 37,0%, Phosphate 95,1%, sulfate 41,7% and COD of 66,7% and reduced the number of microorganisms to a value less than the detectable limit of the analysis method. All mean values obtained for the physicochemical parameters meet the standards required by the Order 2914/2011 of the Ministry of Health for drinking water.

CAPES / A escassez, deterioração da qualidade dos mananciais e o aumento da demanda por água tem sido problema global. Diante desses problemas o uso de fontes alternativas é citado como solução, com destaque para o aproveitamento de água da chuva. Em alguns locais, a água da chuva escoada de telhados tem sido utilizada para fins potáveis e não potáveis e a água da chuva in natura tem qualidade superior ao de águas superficiais e subterrâneas. Embora a água da chuva tenha qualidade físico-química dentro dos padrões de potabilidade, é necessário melhorar sua qualidade para utilizá-la. Assim neste trabalho é avaliado o tratamento da água da chuva por filtro ascendente (volume de 35,4 L) com meio suporte de 0,50 m de seixo rolado e camada filtrante composta de 0,15m de brita, 0,25 m de areia e 0,55 m de carvão ativado e desinfecção por radiação UV. Para melhorar a qualidade da água antes de chegar ao filtro foi instalado um dispositivo de primeiro descarte com volume de 41,4 L. A avaliação do tratamento foi realizada através da análise dos parâmetros pH, temperatura, cor, oxigênio dissolvido, turbidez, amônia, nitrito, nitrato, fosfato, sulfato, DQO e coliformes. Os valores médios obtidos para os parâmetros físico-químicos da água após o tratamento foram de 6,7 para o pH, 22,3 °C para a temperatura, 12,5 UPC para cor, 6,7 mg/L para OD, 0,5 UNT para turbidez, 0,2 mg/L para amônia, 0,01 mg/L para nitrito, 1,7 mg/L para nitrato, 0,2 mg/L para fosfato, 0,7 mg/L para sulfato e 1,3 mg/L para DQO. O tratamento proposto obteve resultados de eficiência para remoção de cor de 22,4%, turbidez de 28,6%, amônia de 50,0%, nitrito de 23,1%, nitrato de 37,0%, fosfato de 95,1% sulfato de 41,7% e DQO de 66,7% e reduziu o numero de microrganismos para um valor menor que o limite detectável do método de análise. Todos os valores médios obtidos para os parâmetros físico-químicos atendem aos padrões exigidos pela portaria 2914/2011 do Ministério da Saúde para água potável. / The scarcity, quality deterioration of water sources and increasing demand for water has been global problem. Faced with these problems the use of alternative sources is cited as a solution, especially taking advantage of rainwater. In some places, rainwater drained roofs have been used for potable and non-potable purposes and rainwater in nature has superior quality to the surface water and groundwater. Although rainwater has physicochemical quality within the potability standards, it is necessary to improve their quality to use it. Thus this work is evaluated treatment of rainwater by upflow filter (35,4 L volume) with support means of 0,50 m of Boulder and filter layer of 0,15 m of crushed stone, 0,25 m of sand and 0,55 m of activated carbon and UV disinfection. To enhance the water quality before reaching the filter was installed a first-flush device with volume of 41,4 L. The characterization of the water before and after treatment was performed through analysis of parameters pH, temperature, color, dissolved oxygen, turbidity, ammonia, nitrite, nitrate, phosphate, sulphate, COD and coliforms. The mean values obtained for the physicochemical parameters of the water after treatment were 6,7 to pH 22,3 °C for temperature, 12,5 UPC for color, 6,7 mg/L to OD, 0,5 NTU for turbidity, 0,2mg/L for ammonia, 0,01 mg/L for nitrite, 1,7 mg/L for nitrate, 0,2 mg/L for phosphate,0,7 mg/L for sulfate and 1,3 mg/L for COD. The obtained results proposed treatment for color removal efficiency of 22,4%, haze 28,6%, 50,0% ammonia, 23,1% nitrite, nitrate 37,0%, Phosphate 95,1%, sulfate 41,7% and COD of 66,7% and reduced the number of microorganisms to a value less than the detectable limit of the analysis method. All mean values obtained for the physicochemical parameters meet the standards required by the Order 2914/2011 of the Ministry of Health for drinking water.