Remoção de ibuprofeno de águas por oxidação catalítica

A ocorrência e destino de fármacos no ambiente aquático tem vindo a ser reconhecido como um problema emergente em química ambiental. Alguns compostos são resistentes à degradação nas estações de tratamento de águas residuais, ETARs, enquanto que outros, ainda que sofram degradação parcial, continuam a ser lançados nos meios aquáticos em quantidades apreciáveis. O Ibuprofeno, IB, um dos anti­ inflamatórios mais consumidos por todo o mundo, é um dos fármacos mais detectados no meio hídrico. Apesar dos sistemas de tratamento convencionais utilizados nas ETARs removerem até 90% do IB das águas residuais, é frequente o efluente descarregado conter ainda quantidades significativas deste poluente. A presença destes compostos no ambiente deve ser avaliada dado que possuem actividade biológica, mesmo a baixas concentrações. Os processos avançados de oxidação com peróxido de hidrogénio, na presença de catalisadores heterogéneos, permitem melhorar significativamente a remoção deste tipo de compostos em águas. Assim, foi objectivo deste trabalho o estudo da utilização de peróxido de hidrogénio como agente oxidante na remoção de IB em soluções aquosas, na presença de complexo de acetilacetonato de Ni (II) disperso em PDMS ou encapsulado em zeólitos NaY. Para o doseamento do fármaco em solução foi necessário desenvolver um método analítico consistindo de separação cromatográfica por HPLC e detecção e quantificação por UV-Vis. Não houve necessidade de recorrer a um passo de pré­ concentração de amostras por extracção em fase sólida (SPE) devido ao facto das concentrações de IB medidas ao longo do trabalho se terem sempre encontrado acima do LOQ (811 g L-1) do método analítico por injecção directa. Deste estudo pode concluir-se que o catalisador que apresentou melhor actividade catalítica e consequentemente maior remoção do IB em solução, foi o complexo de acetilacetonato de Ni (II), disperso em PDMS. Foi avaliada a influência, na conversão do IB, de diferentes parâmetros como a concentração inicial de peróxido de hidrogénio adicionada, quantidade de catalisador utilizada na mistura reaccional e temperatura. Os resultados permitiram concluir que os aumentos destes parâmetros conduzem a um aumento da actividade catalítica da reacção. A estabilidade catalítica do acetilacetonato de Ni (II)/PDMS, foi avaliada em ensaios consecutivos com a mesma amostra e nas mesmas condições, tendo-se observado que, após 8 utilizações, o catalisador perde ligeiramente a actividade (cerca de 11% do seu valor inicial). ABSTRACT: The presence and fate of pharmaceuticals in the aquatic environment is an emergent issue in environmental chemistry. Some compounds are poorly removed in wastewater treatment plants (WWTPs) while others, in spite of being partially removed, are still present in the WWTPs effluents and discharged in the receiving water bodies. Ibuprofen, IB, a non-steroid anti-inflammatory drug, is one of the most used and also one of the most frequently detected pharmaceutical contaminants in aquifers worldwide. Its removal by conventional wastewater treatment processes used in most WWTPs is usually high (up to 90% of incoming IB may be removed), but duet the high loads present in the influents, still significant amounts of IB usually leave the WWTPs in the treated effluents. The presence of these compounds in the environment must be evaluated considering that they may have some biological activity even at low concentrations. Advanced oxidation processes using hydrogen peroxide, in the presence of heterogeneous catalysts, provide a significantly improved removal of this type of substances from waters. Therefore, it was the aim of this work to study the use of hydrogen peroxide as an oxidizing agent in the removal of IB from aqueous solutions, in the presence of the catalyst nickel (II) acetylacetonate dispersed in PDMS or encapsulated in the NaY zeolite. For the quantification of the pharmaceutical in aqueous solution it was necessary to develop an analytical methodology based in chromatographic separation by HPLC and with UV-Vis detection and quantification. There was no need for a pre­concentration step of the samples by solid phase extraction (SPE) as the IB concentrations measured were always above the limit of quantification (811 bL1 of) the analytical method. The results from this study have shown that the catalyst which presented the best catalytic activity and the highest IB removal in solution was nickel (II) acetylacetonate dispersed in PDMS.

Biodiesel production from waste cooking oil over sulfonated catalysts

Biodiesel production from waste cooking oil with methanol was carried out in the presence of poly(vinyl alcohol) with sulfonic acid groups (PVA-SO3H) and polystyrene with sulfonic acid groups (PS-SO3H), at 60°C. The PVA-SO3H catalyst showed higher catalytic activity than the PS-SO3H one. In order to optimize the reaction conditions, different parameters were studied. An increase of waste cooking oil conversion into fatty acid methyl esters with the amount of PVA-SO3H was observed. When the transesterification and esterification of WCO was carried out with ethanol over PVA-SO3H, at 60°C, a decrease of biodiesel production was also observed. The WCO conversion into fatty acid ethyl ester increased when the temperature was increased from 60 to 80°C. When different amounts of free fatty acids were added to the reaction mixture, a slight increase on the conversion was observed. The PVASO3H catalyst was reused and recycled with negligible loss in the activity.

Composites Chitosan/SBA-15 with sulfonic acid as heterogeneous catalysts for biodiesel production

Free fatty acids (palmitic, stearic and oleic acid) were converted into biodiesel with methanol over composites catalysts consisting in SBA-15 with sulfonic acid groups (SBA-15-SO3H) immobilized in Chitosan (CH), at 60ºC. It was observed that the catalytic activity increased with the amount of SBA-15-SO3H dispersed in CH. It was also observed that the catalytic activity decreased in the series: palmitic acid > stearic acid > oleic. The catalytic stability of [SBA-15-SO3H]3/CH composites was studied. A good stability was observed.

Photocatalytic production of chemicals and hydrogen from biomass

In this work, with the aim to tackle several approaches towards sustainable chemistry, two reactions were studied: aerobic photo-oxidation of biomass derived 5-hydroxymethyl-2-furfural (HMF), and anaerobic photo-reforming of glycerol known as a by-product in biodiesel industry, towards production of chemicals and hydrogen. Solar-assisted reactions were performed by means of heterogeneous photocatalysis, in mild conditions such as atmospheric pressure, room temperature and water as a benign solvent. Titanium dioxide (lab-synthesized and commercial) was used as a photo-active catalyst, which surface was modified by introducing different metal (e.g. Au, Au-Cu, Pt) and metal oxide (e.g. NiO) nanoparticles. The prepared materials were characterized by XRD, DRS, BET, TEM, SEM, RAMAN and other techniques. The influence of the support, the size and type of the deposited metal and metal oxide nanoparticles on the photo-catalytic transformation of HMF and glycerol was evaluated. In the case of HMF, the influence of the base addition and the oxygen content on the reaction selectivity was also studied. The effect of the crystalline phase composition and morphology of TiO2 in the glycerol photo-reforming reaction was assessed as well. The surface of the synthesized TiO2 nano-powders was investigated by means of Surface Organometallic Chemistry (SOMC) approach. In particular, the surface was characterized by chemical titration and DRIFT techniques. Furthermore, the SOMC concept allowed preparing of well-dispersed Pt nanoparticles on the TiO2 surface. The photo-catalytic activity of this sample in the glycerol photo-reforming process was tested and compared to that of other Pt-containing catalysts prepared by conventional technics. In view of avoiding the agglomeration and sedimentation of suspended titania powders in water media, thick films of synthesized and commercial TiO2 were deposited on a conductive substrate using screen-printing technique. The prepared electrodes were characterized by profilometry, SEM, XRD, optical, electrochemical and photo-electrochemical methods.

Nuovi processi catalitici per la produzione di syngas

The study of the combined Steam/Dry Reforming (S/DR) process for the production of syngas (CO + H2) from clean biogas was carried out using Ni/Ir bimetallic catalysts on Mg and Al mixed-oxides, obtained by calcination of hydrotalcite-type precursors (Ht) prepared by co-precipitation. The presence of small amounts of Ir promoted the catalytic activity and limited the deactivation phenomena through the formation of a bimetallic alloy, which does the catalyst very active even at lowest temperature and in lack of steam. By integrating a High Temperature–WGS unit (HTS) after the S/DR reactor it was possible to increase the H2 yield of the process. The performance of the Zn/Al/Cu-based catalyst was improved using a templating agent during the synthesis of the catalyst, which increased the catalyst’s structural properties and activity especially at lowest temperatures and at highest contact times. Finally, starting from the laboratory data, it was possible to simulate the S/DR process on industrial scale, evaluating its scalability and environmental impact. The results showed that, using the S/DR technology instead of the current processes, it was possible to reduce the energy costs and the atmospheric emissions of the plant.

Studio del reforming combinato del biogas su nanoparticelle bimetalliche supportate

The study of the combined reforming (CR) process to produce synthesis gas (CO + H2) feeding Clean Biogas (CB, biogas in which the main pollutants have been removed) has been performed on Ni-based bimetallic catalysts promoted by small amounts of Rh or Cu, prepared by incipient wetness impregnation or coprecipitation of different precursors on mixed oxides Mg/Al/O obtained by calcination of hydrotalcite-type (Ht) coprecipitates. It has been observed as the formation of bimetallic particles promoted the catalytic activity and limited the deactivation phenomena, allowing to operate at lower temperature and feeding lower amounts of steam. By this way, it was possible to define the best promoter, to tune its amount and the formation of the bimetallic nanoparticles. Finally, it has been simulated the scale-up of the CR process to industrial level, evaluating the feasibility and economic degree by comparison with the industrially exploited Autothermal reforming (ATR) process, evidencing the possible scalability and the advantages at environmental and energetic level in comparison to the current reforming processes.

Multi-functional electrocatalysts for CO2 reduction reaction: towards the modulation of selectivity

The electrocatalytic reduction of CO2 (CO2RR) is a captivating strategy for the conversion of CO2 into fuels, to realize a carbon neutral circular economy. In the recent years, research has focused on the development of new materials and technology capable of capturing and converting CO2 into useful products. The main problem of CO2RR is given by its poor selectivity, which can lead to the formation of numerous reaction products, to the detriment of efficiencies. For this reason, the design of new electrocatalysts that selectively and efficiently reduce CO2 is a fundamental step for the future exploitation of this technology. Here we present a new class of electrocatalysts, designed with a modular approach, namely, deriving from the combination of different building blocks in a single nanostructure. With this approach it is possible to obtain materials with an innovative design and new functionalities, where the interconnections between the various components are essential to obtain a highly selective and efficient reduction of CO2, thus opening up new possibilities in the design of optimized electrocatalytic materials. By combining the unique physic-chemical properties of carbon nanostructures (CNS) with nanocrystalline metal oxides (MO), we were able to modulate the selectivity of CO2RR, with the production of formic acid and syngas at low overpotentials. The CNS have not only the task of stabilizing the MO nanoparticles, but the creation of an optimal interface between two nanostructures is able to improve the catalytic activity of the active phase of the material. While the presence of oxygen atoms in the MO creates defects that accelerate the reaction kinetics and stabilize certain reaction intermediates, selecting the reaction pathway. Finally, a part was dedicated to the study of the experimental parameters influencing the CO2RR, with the aim of improving the experimental setup in order to obtain commercial catalytic performances.

New Gold(I) complexes: from ligand design to homogeneous catalysis

This PhD thesis summarize the work carried out during three years of PhD course. Several thematic concerning gold(I) chemistry are analysed by crossing data from different chemistry areas as: organic chemistry, organometallic chemistry, inorganic chemistry and computational chemistry. In particular, the thesis focuses its attention on the evaluation of secondary electronic interactions, subsisting between ligand and Au(I) metal centre in the catalyst, and their effects on catalytic activity. The interaction that has been taken in consideration is the Au…Ar π-interaction which is known to prevent the decomposition of catalyst, but exhaustive investigations of further effects has never been done so far. New libraries of carbene (ImPy) and biarylphosphine ligands have been designed and synthetized for the purpose and subsequently utilized for the synthesis of corresponding Au(I) complexes. Resulting catalysts are tested in various catalytic processes involving different intermediates and in combination with solid state information from SC-XRD revealed an unprecedented activation mode which is only explained by considering both electronic nature and strength of Au…Ar π-interaction. DFT calculation carried on catalysis intermediates are in agreement with experimental ones, giving robustness to the theory. Moreover, a new synthetic protocol for the lactonization of N-allenyl indole-2-carboxylic acids is presented. Reaction conditions are optimized with the newly synthetized ImPy-Au(I) catalysts and different substrates are also tested providing a quite broad reaction scope. Chiral ImPy ligands have also been developed for the asymmetric variant of the same reaction and encouraging enantiomeric excess are obtained.

Investigation on the role of polymeric ligands in heterogeneous nanocatalysis towards the development of hybrid metal-polymer catalysts

The relationship between catalytic properties and the nature of the active phase is well-established, with increased presence typically leading to enhanced catalysis. However, the costs associated with acquiring and processing these metals can become economically and environmentally unsustainable for global industries. Thus, there is potential for a paradigm shift towards utilizing polymeric ligands or other polymeric systems to modulate and enhance catalytic performance. This alternative approach has the potential to reduce the requisite amount of active phase while preserving effective catalytic activity. Such a strategy could yield substantial benefits from both economic and environmental perspectives. The primary objective of this research is to examine the influence of polymeric hydro-soluble ligands on the final properties, such as size and dispersion of the active phase, as well as the catalytic activity, encompassing conversion, selectivity towards desired products, and stability, of colloidal gold nanoparticles supported on active carbon. The goal is to elucidate the impact of polymers systematically, offering a toolbox for fine-tuning catalytic performances from the initial stages of catalyst design. Moreover, investigating the potential to augment conversion and selectivity in specific reactions through tailored polymeric ligands holds promise for reshaping catalyst preparation methodologies, thereby fostering the development of more economically sustainable materials.

The catalytic and other residues essential for the activity of the midgut trehalase from Spodoptera frugiperda

Trehalase (EC 3.2.1.28) hydrolyzes only alpha, alpha`- trehalose and is present in a variety of organisms, but is most important in insects and fungi. Crystallographic data showed that bacterial trehalase has 0312 and E496 as the catalytical residues and three Arg residues in the active site. Those residues have homologous in all family 37 trehalases including Spodoptera frugiperda trehalase (0322, E520, R169, R227, R287). To test the role of these residues, mutants of trehalase were produced. All mutants were at least four orders of magnitude less active than wild type trehalase and no structural difference between these mutants and wild type enzyme were discernible by circular dichroism. D322A and E520 pH-activity profile lacked the alkaline arm and the acid arm, respectively, suggesting that D322 is the acid and E520 the basic catalyst. Azide increases E520A activity three times, confirming its action as the basic catalyst. Taking into account the decrease in activity after substitution for alanine residue, the three arginine residues are as important as the catalytical ones to trehalase activity. This clarifies the previous misidentification of an Arg residue as the acid catalyst. As far as we know, this is the first report on the functional identification residues important for trehalase activity. (C) 2010 Elsevier Ltd. All rights reserved.

A glutamate residue in the catalytic center of the yeast chorismate mutase restricts enzyme activity to acidic conditions

Chorismate mutase acts at the first branchpoint of aromatic amino acid biosynthesis and catalyzes the conversion of chorismate to prephenate. Comparison of the x-ray structures of allosteric chorismate mutase from the yeast Saccharomyces cerevisiae with Escherichia coli chorismate mutase/prephenate dehydratase suggested conserved active sites between both enzymes. We have replaced all critical amino acid residues, Arg-16, Arg-157, Lys-168, Glu-198, Thr-242, and Glu-246, of yeast chorismate mutase by aliphatic amino acid residues. The resulting enzymes exhibit the necessity of these residues for catalytic function and provide evidence of their localization at the active site. Unlike some bacterial enzymes, yeast chorismate mutase has highest activity at acidic pH values. Replacement of Glu-246 in the yeast chorismate mutase by glutamine changes the pH optimum for activity of the enzyme from a narrow to a broad pH range. These data suggest that Glu-246 in the catalytic center must be protonated for maximum catalysis and restricts optimal activity of the enzyme to low pH.

In vivo activity in a catalytic antibody-prodrug system: Antibody catalyzed etoposide prodrug activation for selective chemotherapy

Effective chemotherapy remains a key issue for successful cancer treatment in general and neuroblastoma in particular. Here we report a chemotherapeutic strategy based on catalytic antibody-mediated prodrug activation. To study this approach in an animal model of neuroblastoma, we have synthesized prodrugs of etoposide, a drug widely used to treat this cancer in humans. The prodrug incorporates a trigger portion designed to be released by sequential retro-aldol/retro-Michael reactions catalyzed by aldolase antibody 38C2. This unique prodrug was greater than 102-fold less toxic than etoposide itself in in vitro assays against the NXS2 neuroblastoma cell line. Drug activity was restored after activation by antibody 38C2. Proof of principle for local antibody-catalyzed prodrug activation in vivo was established in a syngeneic model of murine neuroblastoma. Mice with established 100-mm3 s.c. tumors who received one intratumoral injection of antibody 38C2 followed by systemic i.p. injections with the etoposide prodrug showed a 75% reduction in s.c. tumor growth. In contrast, injection of either antibody or prodrug alone had no antitumor effect. Systemic injections of etoposide at the maximum tolerated dose were significantly less effective than the intratumoral antibody 38C2 and systemic etoposide prodrug combination. Significantly, mice treated with the prodrug at 30-fold the maximum tolerated dose of etoposide showed no signs of prodrug toxicity, indicating that the prodrug is not activated by endogenous enzymes. These results suggest that this strategy may provide a new and potentially nonimmunogenic approach for targeted cancer chemotherapy.

Modified silicas covalently bounded to 5,10,15,20-tetrakis(2-hydroxy-5-nitrophenyl)porphyrinato iron(III): synthesis, spectroscopic and EPR characterization. Catalytic studies

In this work we have studied cyclooctene epoxidation with PhIO, using a new iron porphyrin, 5,10,15,20-tetrakis(2-hydroxy-5-nitrophenyl)porphyrinato iron(III), supported on silica matrices via eletrostatic interaction and / or covalent bonds as catalyst. These catalysts were obtained and immobilized on the solid supports propyltrimethylammonium silica (SiN+); propyltrimethylammonium and propylimidazole silica [SiN+(IPG)] and chloropropylsilica (CPS) via elestrostatic interactions and covalent binding. Characterization of the supported catalysts by UV-Vis spectroscopy and EPR (Electron paramagnetic resonance) indicated the presence of a mixture of FeII and FeIII species in all of the three obtained catalysts. In the case of (Z)-cyclooctene epoxidation by PhIO the yields observed for cis-epoxycyclooctane were satisfactory for the reactions catalyzed by the three materials (ranging from 68% to 85%). Such results indicate that immobilization of metalloporphyrins onto solid supports via groups localized on the ortho positions of their mesophenyl rings can lead to efficient catalysts for epoxidation reactions. The catalyst 1-CPS is less active than 1-SiN and 1-SiN(IPG), this argues in favour of the immobilization of this metalloporphyrin onto solids via electrostatic interactions, which is easier to achieve and results in more active oxidation catalysts. Interestingly, the activity of the supported catalysts remained the same even after three successive recyclings; therefore, they are stable under the oxidizing conditions.