Propriedades nanoestruturais de géis de sílica preparados com adiçoes de surfactante anionico

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Adsorção de cromo hexavalente por carvão ativado granulado comercial na presença de surfactante aniônico (LAS)

A remoção de cromo hexavalente de soluções de surfactante aniônico (LAS) por carvão ativado granulado (CAG) comercial foi estudada. Na caracterização do CAG foram empregados métodos padronizados ASTM (diâmetro médio de Sauter, dDMS e pH) e método BET (S, área superficial específica). Os grupos de superfície e PCZ do adsorvente foram determinados, pelo método de Boehm e titulação potenciométrica, respectivamente. Os resultados da caracterização do adsorvente: dDMS=2,4 mm; pH=9,0; S=677,4 m² g-1; grupos básicos (70%) comparados com os grupos ácidos e o PCZ no intervalo de (4,8-8,6). Os ensaios de adsorção do surfactante LAS foram realizados em mesa agitadora (140 rpm/24 h./27 oC); 2,0 g CAG/50 mL de solução, as concentrações do LAS foram determinadas, pelo método padrão do azul de metileno. Os resultados obtidos da remoção percentual em função da concentração inicial e da remoção percentual em função da variação do tempo em todas as concentrações de LAS estudadas foram superiores a 99 %. Os ensaios de adsorção do metal Cr(VI) (5 – 20 mg/L) foram realizados em banho termostático (140 rpm/27 oC); 2,0 g CAG/50 mL de solução; 1 e 24 horas de processo e sem e com adição de surfactante (70; 140; 210; 280; 350; 533 e 700 mg/L). As concentrações iniciais e residuais de metal foram determinadas pelo método colorimétrico da 1,5 difenilcarbazida. A adsorção do metal, sem a adição de LAS não foi satisfatória, a remoção foi em torno de 15%. O percentual de remoção do metal com adição surfactante atingiu valores, em torno de 70% para a menor concentração do metal (5 mg/L) e entre (58 – 65%) paras as demais concentrações.

Development and Validation of A Stability-Indicating Mekc Method for Determination of Flucloxacillin Sodium in Capsules

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Structure and catalytic properties of sulfated zirconia foams

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Avaliação da auto-suficiência energética de reatores anaeróbios no tratamento de esgoto sanitário e água cinza

The anaerobic treatment of sewage is widely employed in Brazil and it is an appreciated way for the treatment of effluents, helping to reduce the environmental impact in rivers. The methane gas obtained from the process can be applied to improve the energetic efficiency of the system, reducing the amount of waste and the cost of the treatment process. This work presents the net energy balance of anaerobic reactors applied to the treatment of sewage. The analysis was performed considering full-scale and laboratory-scale treatment systems. In laboratory scale, the results from three kinds of systems were compared regarding the biological treatment of greywater. Two of them (UASB7 and UASB12) were anaerobic and the other one was a combined anaerobic-aerobic system (UASB7/SBR6). Greywater methanization (compared to theoretical maximum) was calculated considering 100% removal (g BOD/day), the literature percentage removal and the anionic surfactant presence in the effluentt. For each of these three cases, the efficiencies were, respectively, 16.9%, 43.6% and 51.3% in UASB7 reactor, 25.6%, 50.3% and 59.2% in UASB12 reactor and 30.6%, 61.2% and 71.9% in UASB7/SBR6 reactor. The energetic potential was found to be 4.66x10-4, 7.77x10-4 and 5.12x10-4 kWh/L for the UASB7, UASB12 and UASB7/SBR6 reactors, respectively. The pumping system, the aeration (in the anaerobic-aerobic system) and the temperature controlled heating system were considered to calculate the energetic consumption. However, the third one was not employed since tropical regions like Brazil do not need heating systems and also because of its high energetic consumption. The calculated net energy balance in the reactors was negative in the case of greywater, respectively -0.16, -0.28 and -0.18 kWh/L for the reactors UASB7, UASB12 and UASB7/SRB6. In full scale (ETE Jardim das Flores - Rio Claro, SP), the average energy... (Complete abstract click electronic access below)

Efeito do ambiente alterado no epitélio da escama, nas brânquias e na alimentação de Prochilodus lineatus

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Características estruturais de aerogéis hidrofílicos e hidrofóbicos de sílica modificados com Dodecil Sulfato de Sódio

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Interaction of giant extracellular Glossoscolex paulistus hemoglobin (HbGp) with ionic surfactants: A MALDI-TOF-MS study

The giant extracellular hemoglobin of Glossoscolex paulistus (HbGp) is constituted by approximately 144 subunits containing heme groups with molecular masses in the range of 16-19 kDa forming a monomer (d) and a trimer (abc), and around 36 non-heme structures, named linkers (L). Matrix-assisted laser desorption/ionization time-of-flight (MALDI-TOF-MS) analysis was performed recently, to obtain directly information on the molecular masses of the different subunits from HbGp in the oxy-form. This technique demonstrated structural similarity between HbGp and the widely studied hemoglobin of Lumbricus terrestris (HbLt). Indeed, two major isoforms (d(1) and d(2)) of identical proportions with masses of 16,355+/-25 and 16,428+/-24 Da, respectively, and two minor isoforms (d(3) and d(4)) with masses around 16.6 kDa were detected for monomer d of HbGp. In the present work, the effects of anionic sodium dodecyl sulfate (SDS) and cationic cethyltrimethyl ammonium chloride (CTAC) on the oligomeric structure of HbGp have been studied by MALDI-TOF-MS in order to evaluate the interaction between ionic surfactants and HbGp. The data obtained with this technique show an effective interaction of cationic surfactant CTAC with the two isoforms of monomer d, d(1) and d(2), both in the whole protein as well as in the pure isolated monomer. The results show that up to 10 molecules of CTAC are bound to each isoform of the monomer. Differently, the mass spectra obtained for SDS-HbGp system showed that the addition of the anionic surfactant SDS does not originate any mass increment of the monomeric subunits, indicating that SDS-HbGp interaction is, probably, significantly less effective as compared to CTAC-HbGp one. The acid pI of the protein around 5.5 is, probably, responsible for this behavior. The results of this work suggest also some interaction of both surfactants with linker chains as well as with trimers, as judged from observed mass increments. Our data are consistent with a recent spectroscopic study showing a strong interaction between CTAC and HbGp at physiological pH [P.S.Santiago, et al, Biochim. Biophys. Acta. 1770 (2007) 506-517.]. (C) 2007 Elsevier B.V. All rights reserved.

Formation of oxysulfide LnO(2)S(2) and oxysulfate LnO(2)SO(4) phases in the thermal decomposition process of lanthanide sulfonates (Ln = La, Sm)

This study investigates two lanthanide compounds (La(3+) and Sm(3+)) obtained in water/ethyl alcohol solutions employing the anionic surfactant diphenyl-4-amine sulfonate (DAS) as ligand. Both sulfonates were characterized through IR, TG/DTG (O(2) and N(2)). The thermal treatment of both compounds at 1273 K under air leaves residues containing variable percentages of lanthanide oxysulfide/oxysulfate phases shown by synchrotron high-resolution XRD pattern including the Rietveld analysis. The phase distributions found in the residues evidence the differences in the relative stability of the precursors.

Adsorption of Sodium Dodecyl Sulfate on Ge Substrate: The Effect of a Low-Polarity Solvent

This paper describes the adsorption of sodium dodecyl sulfate (SDS) molecules in a low polar solvent on Ge substrate by using Fourier transform infrared-attenuated total reflection (FTIR-ATR) spectroscopy and atomic force microscopy (AFM). The maximum SDS amount adsorbed is (5.0 +/- 0.3) x 10(14) molecules cm(-2) in CHCl3, while with the use of CCl4 as subphase the ability of SDS adsorbed is 48% lower. AFM images show that depositions are highly disordered over the interface, and it was possible to establish that the size of the SDS deposition is around 30-40 nm over the Ge surface. A complete description of the infrared spectroscopic bands for the head and tail groups in the SDS molecule is also provided.

Synthese und Charakterisierung von Polymethylmethacrylat (PMMA)-Silika-Komposit-Partikeln und fluorierten Nanopartikeln unter Verwendung des Miniemulsionsprozesses

In der vorliegenden Dissertation wurden zwei verschiedene Fragestellungen bearbeitet. Zum einen wurde im Rahmen des Schwerpunktprojektes „Kolloidverfahrenstechnik“ und in Zusammenarbeit mit der Arbeitsgruppe von Prof. Dr. Heike Schuchmann vom KIT in Karlsruhe die Verkapselung von Silika-Nanopartikeln in eine PMMA-Hülle durch Miniemulsionspolymerisation entwickelt und der Aufskalierungsprozess unter Verwendung von Hochdruckhomogenisatoren vorangetrieben. Zum anderen wurden verschiedene fluorierte Nanopartikel durch den Miniemulsionsprozess generiert und ihr Verhalten in Zellen untersucht.rnSilika-Partikel konnten durch Miniemulsionspolymerisation in zwei unterschiedlichen Prozessen erfolgreich verkapselt werden. Bei der ersten Methode wurden zunächst modifizierte Silika-Partikel in einer MMA-Monomerphase dispergiert und anschließend durch den normalen Miniemulsionsprozess Silika-beladene Tröpfchen generiert. Diese konnten zu Komposit-Partikeln polymerisiert werden. Bei der Verkapselung durch den Fission/Fusion Prozess wurden die hydrophobisierten Silika-Partikel durch Fission und Fusion Prozesse in schon vorhandene Monomertröpfchen eingebracht, welche hinterher polymerisiert wurden. Um hydrophiles Silika in einem hydrophoben Monomer zu dispergieren, musste zunächst eine Modifizierung der Silika-Partikel stattfinden. Dies geschah unter anderem über eine chemische Anbindung von 3-Methacryloxypropyltri-methoxysilan an der Oberfläche der Silika-Partikel. Des Weiteren wurden die hydrophilen Silika-Partikel durch Adsorption von CTMA-Cl physikalisch modifiziert. Unter anderem durch die Variation des Verkapselungsprozesses, der Silika-Menge, der Tensidart und –menge und der Comonomere konnten Komposit-Partikel mit unterschiedlichen Morphologien, Größen, und Füllgraden erhalten werden.rnFluorierte Nanopartikel wurden erfolgreich über den Prozess der Miniemulsionspolymerisation synthetisiert. Als Monomere dienten dabei fluorierte Acrylate, fluorierte Methacrylate und fluoriertes Styrol. Es war möglich aus jeder dieser drei Gruppen an Monomeren fluorierte Nanopartikel herzustellen. Für genauere Untersuchungen wurden 2,3,4,5,6-Pentafluorstyrol, 3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-Heptadecafluorodecyl-methacrylat und 1H,1H,2H,2H-Perfluorodecylacrylat als Monomere ausgewählt. Als Hydrophob zur Unterdrückung der Ostwaldreifung wurde Perfluromethyldecalin eingesetzt. Die stabilsten Miniemulsionen wurden wiederum mit den ionischen Tensid SDS generiert. Mit steigendem Gehalt an SDS gelöst in der kontinuierlichen Phase, wurde eine Verkleinerung der Partikelgröße festgestellt. Neben den Homopolymerpartikeln wurden auch Copolymerpartikel mit Acrylsäure erfolgreich synthetisiert. Zudem wurde noch das Verhalten der fluorierten Partikel in Zellen überprüft. Die fluorierten Partikel wiesen ein nicht toxisches Verhalten vor. Die Adsorption von Proteinen aus Humanem Serum wurde über ITC Messungen untersucht. rnSomit konnte gezeigt werden, dass die Technik der Miniemulsionspolymerisation eine abwechslungsreiche und effektive Methode ist, um Hybridnanopartikel mit verschiedenen Morphologien und oberflächenfunktionalisierte Nanopartikel erfolgreich zu generieren.rn

Metal-complex ionosilicas: Cationic mesoporus silica with Ni(II) and Cu(II) complexes in their framework

Metal-complex ionosilicas with cationic complexes into the mesoporous silica framework were prepared using anionic surfactants. The electrostatic interaction between the anionic surfactant and the cationic metal complexes incorporated in the silica framework allows for the fine tuning of the mesoporous structure. The gentle procedure of synthesis developed and mild ion-exchange extraction of the surfactant, allowed a cleaner route for the immobilization of homogeneous cationic catalysts in mesoporous silica, while protecting the structural and chemical integrity of the metal complexes.

Synthesis of wormlike nanoporous nickel oxide with nanocrystalline framework for electrochemical energy storage

In this work, nanoporous nickel oxide was synthesized using anionic surfactant assembly method. Structure characterizations show that this nickel oxide possesses partly-ordered mesoporous structure with nanocrystalline pore wall. The formation mechanism of wormlike nanoporous structure is ascribed to the quasi-reverse micelle system formed by ternary phases of SDS (sodium dodecyl sulfate)/urea/water. Cyclic voltammetry shows that these nickel oxide samples possess both good capacitive behavior due to its unique nanoporous structure and very high specific capacitance due to its high surface area with electrochemical activity.

The influence of the chemical nature of dispersed phase on stability in oil-in-water emulsions

Some of the problems arising from the inherent instability of emulsions are discussed. Aspects of emulsion stability are described and particular attention is given to the influence of the chemical nature of the dispersed phase on adsorbed film structure and stability, Emulsion stability has been measured by a photomicrographic technique. Electrophoresis, interfacial tension and droplet rest-time data were also obtained. Emulsions were prepared using a range of oils, including aliphatic and aromatic hydrocarbons, dispersed In a solution of sodium dodecyl sulphate. In some cases a small amount of alkane or alkanol was incorporated into the oil phase. In general the findings agree with the classical view that the stability of oil-in-water emulsions is favoured by a closely packed interfacial film and appreciable electric charge on the droplets. The inclusion of non-ionic alcohol leads to enhanced stability, presumably owing to the formation of a "mixed" interfacial film which is more closely packed and probably more coherent than that of the anionic surfactant alone. In some instances differences in stability cannot he accounted for simply by differences in interfacial adsorption or droplet charge. Alternative explanations are discussed and it is postulated that the coarsening of emulsions may occur not only hy coalescence but also through the migration of oil from small droplets to larger ones by molecular diffusion. The viability of using the coalescence rates of droplets at a plane interface as a guide to emulsion stability has been researched. The construction of a suitable apparatus and the development of a standard testing procedure are described. Coalescence-time distributions may be correlated by equations similar to those presented by other workers, or by an analysis based upon the log-normal function. Stability parameters for a range of oils are discussed in terms of differences in film drainage and the natl1re of the interfacial film. Despite some broad correlations there is generally poor agreement between droplet and emulsion stabilities. It is concluded that hydrodynamic factors largely determine droplet stability in the systems studied. Consequently droplet rest-time measurements do not provide a sensible indication of emulsion stability,

Remoção de corantes utilizando tensoativos: extração por ponto de nuvem e floculação iônica

The textile sector is one of the main contributors to the generation of industrial wastewaters due to the use of large volumes of water, which has a high organic load content. In these, it is observed to the presence of dyes, surfactants, starch, alcohols, acetic acid and other constituents, from the various processing steps of the textiles. Hence, the treatment of textile wastewater becomes fundamental before releasing it into water bodies, where they can cause disastrous physical-chemical changes for the environment. Surfactants are substances widely used in separation processes and their use for treating textile wastewaters was evaluated in this research by applying the cloud point extraction and the ionic flocculation. In the cloud point extraction was used as surfactant nonylphenol with 9.5 ethoxylation degree to remove reactive dye. The process evaluation was performed in terms of temperature, surfactant and dye concentrations. The dye removal reached 91%. The ionic flocculation occurs due to the presence of calcium, which reacts with anionic surfactant to form insoluble surfactants capable of attracting the organic matter by adsorption. In this work the ionic flocculation using base soap was applied to the treatment of synthetic wastewater containing dyes belonging to three classes: direct, reactive, and disperse. It was evaluated by the influence of the following parameters: surfactant and electrolyte concentrations, stirring speed, equilibrium time, temperature, and pH. The flocculation of the surfactant was carried out in two ways: forming the floc in the effluent itself and forming the floc before mixing it to the effluent. Removal of reactive and direct dye, when the floc is formed into textile effluent was 97% and 87%, respectively. In the case where the floc is formed prior to adding it to the effluent, the removal to direct and disperse dye reached 92% and 87%, respectively. These results show the efficience of the evaluated processes for dye removal from textile wastewaters.