Leaching of metals from red mud and toxicity in human cells in vitro.

Toxicity of red mud, a waste from alumina production, was studied using human breast cancer MCF-7 cells. Culture medium was prepared by mixing water for 3 days with the red mud and removing solid particles afterwards (red mud water). Culture for 48 h of the cells in this medium in neutral pH decreased the cell viability, as analyzed by the MTT-test, and increased the formation of reactive oxygen species. Thus, neutralization does not eliminate the toxicity of red mud. In preliminary experiments, a combined effect of five metals (Cr, Li, V, Al, As) increased the formation of ROS (reactive oxygen species) statistically significantly. Each element separately did not have a similar effect. In environmental applications, red mud is likely to be used after activation. In this work, the red mud was activated using hydrochloric acid to study the physical and chemical properties before and after the treatment. Activation increased the specific surface area of red mud from 16 m2 g-1 to 148 m2 g-1, which is beneficial in many environmental applications such as in the adsorptive removal of pollutants. After activation, leaching of some elements from the red mud decreased (e.g. Al from 38.0 to 0.56 mg L-1, As from 21.0 to 2.1 µg L-1, V from 172.0 to 29.8 µg L-1) while some increased (e.g. Li from 0.04 to 2.81 mg L-1, Cr from 0.35 to 3.23 mg L-1).

Caracterización de filtros comerciales para agua a base de carbón activado para el tratamiento de agua del río Tumbes - Perú / Characterization of water commercial filters based on activated carbon for water treatment of the Tumbes river - Peru / Caracterização de carvão ativado de filtros comerciais para tratamento da água do rio Tumbes -Perú

Resumen Se caracterizaron y se evaluaron carbones activados comerciales (A, B, C y D) utilizados en filtros para el tratamiento de agua en la descontaminación de metales pesados presentes en agua de río y en la eliminacion de microorganismos coliformes; los carbones comerciales resultaron tener estructuras microporosas y mesoporosas. Se determinaron areas superficiales entre 705 y 906 m2/g. Los carbones fueron amorfos y se detectó la presencia de agentes antibacterianos, tales como Ag, Cl, Cu y Si. Se determinó que para el As y Pb, cuyas concentraciones iniciales en el agua contaminada (agua del Río Tumbes-Perú) fueron 56,7 y 224,0 μg/L, respectivamente, el porcentaje de adsorción fue cercano al 100%. También se encontró que la relación entre el pH de carga cero de los carbones y pH del agua del río durante los experimentos juega un rol determinante en la adsorción de los elementos analizados. Por otro lado, la capacidad antibacteriana fue evaluada satisfactoriamente frente a las siguientes cepas de bacterias gram negativas fecales: Escherichia coli (ATCC® 25922™), Salmonella typhimurium (ATCC® 14028™) y Shigella flexneri (ATCC® 12022™). Esta capacidad se basa en la presencia superficial en los carbones de los agentes antibacterianos mencionados.

Abstract Comercial activated carbon samples (A, B, C, and D) used in filters for the treatment of water were characterized and evaluated in the decontamination of heavy metals present in river water and in the elimination of coliform microorganisms. The carbon samples had microporous and mesoporous structures. Surface areas of between 705 and 906 m2/g were found. The carbon samples were amorphous and the presence of antibacterial agents such as Ag, Cl, Cu, and Si was detected. It was determined that for As and Pb, whose initial concentrations in contaminated water (water of the Tumbes river-Peru) were 56.7 and 224.0 μg/L, respectively, the percentage of adsorption was close to 100%. The relationship between point of zero charge pH of the activated carbons and pH of the river water during the experiments plays a determinant role in the adsorption of the analyzed elements. The antibacterial capacity was evaluated satisfactorily against the following strains of fecal gram negative bacteria: Escherichia coli (ATCC® 25922™), Salmonella typhimurium (ATCC® 14028™), and Shigella flexneri (ATCC® 12022™). This ability is based on the surface presence in the carbons ofthe mentioned antibacterial agents.

Resumo Carvões ativados comerciais (A, B, C e D) usado em filtros para o tratamento de água foram caracterizados e avaliados na descontaminação de metais pesados da água do rio e para a remoção de microrganismos coliformes. Os carvões comerciais mostraram estruturas microporosas e mesoporosas. Foram determinadas as áreas superficiais entre 705 e 906 m2/g. As amostras de carvão foram amorfas e foi detectada a presença de agentes antibacterianos, tais como Ag, Cl, Cu e Si. Determinou-se que, no caso de As e Pb, cujas concentrações iniciais na água contaminada (água do rio Tumbes-Peru) foram de 56,7 e 224,0 μg/L respectivamente, a taxa de adsorção foi de quase 100%. Também foi econtrado que e a relação entre o pH de carga zero dos carvões e o pH da água do rio durante as experiências desempenha um papel decisivo na adsorção dos elementos analisados. Além disso, a capacidade antibacteriana foi avaliada com sucesso contra as seguintes variedades de bactérias gram negativas de origem fecal: Escherichia coli (ATCC® 25922™), Salmonella typhimurium (ATCC® 14028™) e Shigella flexneri (ATCC® 12022™). Esta capacidade esta baseada na presença de agentes bacterianos na superfície dos carvões.

Micellar-enhanced ultrafiltration for the removal of cadmium and zinc: Use of response surface methodology to improve understanding of process performance and optimisation.

In this study, removal of cadmium and zinc from their respective water samples was conducted by micellar-enhanced ultrafiltration (MEUF), using sodium dodecyl sulfate (SDS) as the surfactant. Response surface methodology (RSM) was used for modelling and optimising the process, and to gain a better understanding of the process performance. Face Centred Composite (CCF) Design was used as the experimental design. The factors studied were pressure (P), nominal molecular weight limit (NMWL), heavy metal feed concentration (C(Zn), C(Cd)) and SDS feed concentration (C(SDS)). Using RSM the retention of heavy metals was maximized while optimising the surfactant to metal ratio (S/M). Response surface plots improved the understanding the effect of the factors on permeate flux. Concentration polarisation was negligible and therefore, high NMWL membranes with high pressure provided high flux with negligible effect on the retention of heavy metals. The optimal conditions of zinc removal were C(SDS)=13.9 mM, C(Zn)=0.5 mM, NMWL=10 kDa and P=3.0 bar, and for cadmium removal C(SDS)=14.2 mM, C(Cd)=0.5 mM, NMWL=10 kDa and P=3.0 bar. The retentions achieved were 98.0+/-0.4% for zinc and 99.0+/-0.4% for cadmium. To improve resource efficiency, the surfactant was reclaimed after use; 84% of the initial SDS was recovered by precipitation.

Exposure assessment of particulates of diesel and natural gas fuelled buses in silico.

Lung deposition estimates of particulate emissions of diesel and natural gas (CNG) fuelled vehicles were studied by using in silico methodology. Particulate emissions and particulate number size distributions of two Euro 2 petroleum based diesel buses and one Euro 3 gas bus were measured. One of the petroleum based diesel buses used in the study was equipped with an oxidation catalyst on the vehicle (DI-OC) while the second had a partial-DPF catalyst (DI-pDPF). The third bus used was the gas bus with an oxidation catalyst on the vehicle (CNG-OC). The measurements were done using a transient chassis dynamometer test cycle (Braunschweig cycle) and an Electric Low Pressure Impactor (ELPI) with formed particulates in the size range of 7 nm to 10 microm. The total amounts of the emitted diesel particulates were 88-fold for DI-OC and 57-fold for DI-pDPF compared to the total amount of emitted CNG particulates. Estimates for the deposited particulates were computed with a lung deposition model ICRP 66 using in-house MATLAB scripts. The results were given as particulate numbers and percentages deposited in five different regions of the respiratory system. The percentages of particulates deposited in the respiratory system were 56% for DI-OC, 51% for DI-pDPF and 77% for CNG-OC of all the inhaled particulates. The result shows that under similar conditions the total lung dose of particulates originating from petroleum diesel fuelled engines DI-OC and DI-pDPF was more than 60-fold and 35-fold, respectively, compared to the lung dose of particulates originating from the CNG fuelled engine. The results also indicate that a majority (35-50%) of the inhaled particulates emitted from the tested petroleum diesel and CNG engines penetrate deep into the unciliated regions of the lung where gas-exchange occurs.