Tuning the reaction products of ruthenium and ciprofloxacin for studies of DNA interactions

This work presents two potential metallo-drugs, the ionic (C17H19FN3O3)(3)[RuCl6]center dot 3H(2)O (1) and the coordination [Ru(C17H17FN3O3)(3)]center dot 4H(2)O (2) compounds, obtained by the combination of ruthenium(III) and ciprofloxacin in different synthetic conditions. The ESI MS spectrum of 1 displayed a main peak at m/z = 994.6, assigned to the gaseous phase adduct (ciprofloxacin)(3)center dot H+, while 2 featured peaks at m/z 1093.3 and 547.1 ascribed to [Ru(C17H17FN3O3)(3)center dot H+-4H(2)O](+) and [Ru(C17H17FN3O3)(3)center dot 2H(+)-4H(2)O](2+). Thermal analysis corroborated the proposed water content for both complexes. Absorption spectra of the compounds in aqueous medium are dominated by ciprofloxacin transitions in the UV region but displayed weak bands in the visible region, assigned to ligand field transitions. The cyclic voltammograms of 2 exhibited a quasi-reversible process ascribed to the Ru(II)/(III) redox pair at -0.25V (vs. SHE) while 1 displayed this process at -0.11 V, showing that the central ruthenium ion is stabilized in the (III) oxidation state by the coordination to the hard oxygen atoms of ciprofloxacin. The solubility of 1 is pH dependent (as well as free ciprofloxacin) while 2 is fully water soluble and stable under physiological pH for at least 48 h. The compounds are also stable under incubation conditions (stomach pH and 37 degrees C) without significant pH lowering. An interaction study of 2 with ct-DNA showed a value of K-b = 2.47 (+/- 0.89) x 10(4) mol(-1) L for the intrinsic binding constant.

Laboruntersuchungen zur Aufnahme von NH 3 durch Eiskristalle bei Gleichgewicht und beim Wachstum

In dieser Arbeit wurde in Laborexperimenten die Aufnahme von NH3 durch wachsende Eiskristalle und Eiskristalle, die in eisgesättigter Umgebung mit ihrer mittleren Fallgeschwindigkeit angeströmt wurden, untersucht. So sollten die Verhältnisse innerhalb der Wolke beim Wachstum der Eiskristalle “in cloud scavenging“ und unterhalb der Wolke beim Anströmen mit eisgesättigter NH3 - Luftmischung simuliert werden. Bei längerer Exposition dendritischer Eiskristalle mit eisgesättigter NH3 - Luftmischung ist die Diffusion des gebildeten NH4+ in den Eiskristall hinein, entscheidend für den Anteil an NH3, der aus der Gasphase nach der Adsorption als NH4+ im Eis zurückbleibt. Die experimentellen Daten konnten mit einer einfachen Annahme zur Diffusion in einen “halb unendlichen“ Festkörper beschrieben werden. In weiteren Experimenten konnte gezeigt werden, dass die Aufnahme des NH3 durch nicht wachsende Eiskristalle von anderen Spurenstoffen im Eis beeinflusst wird. Eiskristalle, die im Vorfeld des Strömungsadsorptionsexperiments mit NH3, mit SO2 exponiert wurden, zeigten eine deutliche Zunahme der NH3 - Aufnahme aus der Gasphase. Die Aufnahme von NH3 durch nicht wachsende Eiskristalle ist für typische atmosphärische NH3 - Volumenmischungsverhältnisse nicht relevant. Dagegen zeigten die Experimente zur NH3 Aufnahme beim Eiskristallwachstum, dass dieser Prozess in der Atmosphäre nicht vernachlässigt werden kann.

Transport of volatile chlorinated hydrocarbons in unsaturated aggregated media

Transport of volatile hydrocarbons in soils is largely controlled by interactions of vapours with the liquid and solid phase. Sorption on solids of gaseous or dissolved comPounds may be important. Since the contact time between a chemical and a specific sorption site can be rather short, kinetic or mass-transfer resistance effects may be relevant. An existing mathematical model describing advection and diffusion in the gas phase and diffusional transport from the gaseous phase into an intra-aggregate water phase is modified to include linear kinetic sorption on ps-solid and water-solid interfaces. The model accounts for kinetic mass transfer between all three phases in a soil. The solution of the Laplace-transformed equations is inverted numerically. We performed transient column experiments with 1,1,2-Trichloroethane, Trichloroethylene, and Tetrachloroethylene using air-dry solid and water-saturated porous glass beads. The breakthrough curves were calculated based on independently estimated parameters. The model calculations agree well with experimental data. The different transport behaviour of the three compounds in our system primarily depends on Henry's constants.

Recuperação de enxofre elementar a partir de águas residuárias em reatores anaeróbio/microaerado

O objetivo desse projeto de pesquisa foi avaliar a redução do sulfato e promover a remoção do sulfeto, por via de conversão a enxofre elementar, em reatores combinados anaeróbio/microaerado. Para tanto foram utilizados três sistemas com objetivos específicos. A primeira configuração foi um reator anaeróbio de leito fixo e ordenado integrado a um reator microaerado com membrana externa (ABFSB-RME) com o qual se avaliou a influência do tempo de detenção hidráulica (TDH) e da presença de biomassa aderida na remoção do sulfeto. A segunda configuração avaliada foi um reator UASB com um reator microaerado de membrana helicoidal externa (UASB-RMHE), com o qual se avaliou a formação de biofilme no interior da membrana e a alteração do pH para a remoção do sulfeto em sua fase gasosa. A terceira configuração foi um reator anaeróbio de leito fixo e ordenado combinado a um reator microaerado com membrana helicoidal e submersa ao meio liquido (ABFSB-RMHS) com a finalidade de avaliar a remoção do sulfeto com aplicação de fluxo de ar no interior da membrana e avaliar a influência do TDH na eficiência de conversão do sulfeto. Os resultados indicam que a troca periódica das membranas tem influência na eficiência da conversão do sulfeto para o sistema ABFSB-RME. O sistema UASB-RMHE apresentou dados de remoção de sulfeto estáveis durante 35 dias, com remoção de até 90%, porém a retro lavagem da membrana é essencial para o aumento da vida útil do sistema A alteração do pH provocou a deslocamento de equilíbrio do sulfeto, e apresentou remoção do sulfeto no biogás de 98% para pH 7,5 e 50% para pH 7,0. O sistema ABFSB-RMHS propiciou remoção estável de sulfeto e a formação em camadas de enxofre elementar ao redor da membrana que se rompiam permitindo, assim, a sedimentação e recuperação do material sólido. Os resultados obtidos na pesquisa mostraram que os sistemas apresentam viabilidade e potencial no tratamento de águas ricas em compostos de enxofre e para a recuperação de enxofre elementar, além de apresentar versatilidade por meio de variáveis operacionais, com as quais se podem obter o controle e aperfeiçoamento do sistema.

Passive air sampling theory for semivolatile organic compounds

The mathematical modelling underlying passive air sampling theory can be based on mass transfer coefficients or rate constants. Generally, these models have not been inter-related. Starting with basic models, the exchange of chemicals between the gaseous phase and the sampler is developed using mass transfer coefficients and rate constants. Importantly, the inter-relationships between the approaches are demonstrated by relating uptake rate constants and loss rate constants to mass transfer coefficients when either sampler-side or air-side resistance is dominating chemical exchange. The influence of sampler area and sampler volume on chemical exchange is discussed in general terms and as they relate to frequently used parameters such as sampling rates and time to equilibrium. Where air-side or sampler-side resistance dominates, an increase in the surface area of the sampler will increase sampling rates. Sampling rates are not related to the sampler/air partition coefficient (K-SV) when air-side resistance dominates and increase with K-SV when sampler-side resistance dominates.

Valorização de resíduos provenientes da atividade no setor avícola: aplicação do processo de compostagem

O setor avícola, como setor em constante crescimento está associado à produção de elevadas quantidades de resíduos sólidos orgânicos. A crescente taxa de produção de resíduos avícolas leva à necessidade de lhes dar um destino adequado podendo a valorização orgânica, nomeadamente a compostagem, ser uma opção. O presente estudo pretende dar um contributo para o projeto de uma unidade de compostagem numa empresa portuguesa do setor, com valorização dos resíduos produzidos pela mesma, avaliando o potencial de aplicação desta operação de tratamento de resíduos e a qualidade do produto final. Como primeiro passo foi realizada uma caracterização dos resíduos a utilizar de forma a perceber a sua possível influência no processo de degradação. Os ensaios de compostagem foram realizados à escala laboratorial, numa gama de temperatura de 50 a 55ᵒC, utilizando como substrato base uma mistura dos resíduos avícolas, de acordo com os seus quantitativos de produção. Vários potenciais agentes estruturantes foram também testados, como adição ao substrato. A monitorização do processo foi feita com base em análises das fases gasosa (gases de exaustão), sólida (substrato em decomposição) e líquida (lixiviado). A avaliação do processo foi ainda complementada com a caracterização dos produtos finais obtidos, os quais foram ainda sujeitos a testes de fitotoxicidade. Foram observados graus de conversão de matéria orgânica relativamente altos (40-50%), comprovando a aplicabilidade desta operação de tratamento de resíduos. Embora a diferença entre ensaios tenha sido pouco notória, a utilização de uma combinação de cama de aviário e mato destroçado e compostado aparenta ser ligeiramente mais eficiente, enquanto a utilização de casca de eucalipto produziu os piores resultados. Perdas de humidade e de azoto foram as duas situações mais críticas observadas para os vários ensaios, tendo influência tanto sobre o processo como sobre o produto final. Os compostos obtidos revelam baixa qualidade, exibindo valores elevados de pH e condutividade elétrica e elevadas concentrações de metais pesados, tais como cobre e zinco. Supõe-se que as características adversas verificadas estejam associadas à aplicação de quantidades demasiado elevadas de cinza nos substratos, levando à necessidade de redução deste material; estudos adicionais seriam necessários a fim de avaliar as possibilidades de ajuste das quantidades a utilizar, dos diferentes materiais, com o intuito de produzir um produto final com qualidade, respeitando os requisitos legais.

Production of activated carbons from single and mixtures of synthetic polymers

The production of activated carbons (ACs) involves two main steps: the carbonization of the carbonaceous of raw materials at temperatures below 1073 K in the absence of oxygen and the activation had realized at the temperature up to 1173 but the most useful temperature at 1073 K. In our study we used the most common industrial and consumer solid waste, namely PET, alone or blended with other synthetic polymer PAN. By mixing the two polymers in different ratios, an improvement of the yield of the AC production was found and some textural properties were enhanced by comparison with the AC prepared using each polymer separately. When all the samples were exposed through the carbonization process with a pyrolysis the mixture of PAN-PET (1:1w/w) yield around 31.9%, between that obtained with PET (16.9%) or PAN (42.6%) separately. The combine activation, with CO2 at 1073 K, allow ACs with a lower burn-off degree isothermally, when compared with those attained with PET or PAN alone, but with similarly chemicals or textural properties. The resultant ACs are microporous in their nature, as the activation time increase, the PET-PAN mixture AC are characterized by a better developed porous structure, when associated with the AC prepared from PAN. The AC prepared from PET-PAN mixture are characterized by basic surface characteristics, with a pHpzc around 10.5, which is an important characteristic for future applications on acidic pollutants removals from liquid or gaseous phase. In this study we had used the FTIR methods to determine the main functional groups in the surface of the activated carbons. The adsorbents prepared from PAN fibres presents an IR spectrum with similar characteristics to those obtained with PET wastes, but with fewer peaks and bands with less intensity, in particular for the PAN-8240 sample. This can be reflected by the stretching and deformation modes of NH bond in the range 3100 – 3300 cm-1 and 1520 – 1650 cm-1, respectively. Also, stretching mode associated to C–N, C=N, can contributed to the profile of IR spectrum around 1170 cm-1, 1585 – 1770 cm-1. And the TGA methods was used to study the loses of the precursors mass according to the excessive of the temperature. The results showed that, there were different decreasing of the mass of each precursors. PAN degradation started at almost 573 K and at 1073 K, PAN preserve more than 40% of the initial mass. PET degradation started at 650 K, but at 1073 K, it has lost 80% of the initial mass. However, the mixture of PET-PAN (1:1w/w) showed a thermogravimetric profile between the two polymers tested individually, with a final mass slightly less than 30%. From a chemical point of view, the carbonisation of PET mainly occurs in one step between 650 and 775 K.

Testing the effectiveness of phytoscreening to monitor shallow groundwater contamination by chlorinated ethenes

The research presented herein aims to investigate the strengths and weaknesses of a relatively new technique called phytoscreening. Parallel to the well-known phytoremediation, it consists of exploiting the absorbing potential of trees to delineate groundwater contamination plumes, especially for chlorinated ethenes (i.e., PCE, TCE, 1,2-cis DCE, and VC). The latter are prevalent contaminants in groundwater but their fate and transport in surface ecosystems, such as trees, are still poorly understood and subjected to high variability. Moreover, the analytical validity of tree-coring is still limited in many countries due to a lack of knowledge of its application opportunities. Tree-cores are extracted from trunks and generally analyzed by gas chromatography/mass spectrometry. A systematic review of former literature on phytoscreening for chlorinated ethenes is presented in this PhD thesis to evaluate the factors influencing the effectiveness of the technique. Besides, we tested the technique by probing eight sites contaminated by chlorinated ethenes in Italy (Emilia-Romagna) in different hydrogeological and seasonal settings. We coupled the technique with the assessment of gaseous-phase concentrations directly on-site, inserting detector tubes or a photoionization detector in the tree-holes left by the coring tool. Finally, we applied rank order statistic analysis on field data along with literature data to assess under which conditions phytoscreening should be applied to either screen or monitor environmental contamination issues. A relatively high correlation exists between tree-core and groundwater concentrations (Spearman’s ρ > 0.6), being higher for compounds with higher sorption, for sites with shallower and thinner aquifers, and when sampling specific tree types with standardized sampling and extraction protocols. These results indicate the opportunities for assessing the occurrence, type, and concentration of solvents directly from the stem of trees. This can reduce the costs of characterization surveys, allowing rapid identification of hotspots and plume direction and thus optimizing the drilling of boreholes.

Gas-phase solvolysis type reactions of SiCl3+ cations

Gas-phase SiCl3+ ions undergo sequential solvolysis type reactions with water, methanol, ammonia, methylamine and propylene. Studies carried out in a Fourier Transform mass spectrometer reveal that these reactions are facile at 10-8 Torr and give rise to substituted chlorosilyl cations. Ab initio and DFT calculations reveal that these reactions proceed by addition of the silyl cation to the oxygen or nitrogen lone pair followed by a 1,3-H migration in the transition state. These transition states are calculated to lie below the energy of the reactants. By comparison, hydrolysis of gaseous CCl3+ is calculated to involve a substantial positive energy barrier.

Performance evaluation of packing materials in the removal of hydrogen sulphide in gas-phase biofilters: Polyurethane foam, sugarcane bagasse, and coconut fibre

The main objective of this work was to investigate three packing materials (polyurethane foam, sugar-cane bagasse, and coconut fibre) for biofiltration of a gaseous mixture containing hydrogen sulphide (H(2)S). Mixed cultures were obtained from two sources, aerated submerged biofilters and activated sludge, and were utilised as inoculums. Biofilters reached 100% removal efficiency after two clays of operation. The empty bed residence time was 495 for each of the biofilters. The reactors were operated simultaneously, and the inlet concentrations of H(2)S varied between 184 and 644 ppmv during the long-term continuous operation of the biofilters (100 clays). Average removal efficiencies remained above 99.3%, taking into consideration the entire period of operation. Average elimination capacities reached by the biofilters packed with polyurethane foam, coconut fibre, and sugarcane bagasse were in the range of 17.8-66.6; 18.9-68.8, and 18.7-72.9g m(-3) h(-1), respectively. Finally, we concluded that the packing materials tested in this work are appropriate for the long-term biofiltration of hydrogen sulphide. (C) 2010 Elsevier B.V. All rights reserved.

Polycyclic aromatic hydrocarbons in gas and particulate phases of indoor environments influenced by tobacco smoke: levels, phase distributions, and health risks

As polycyclic aromatic hydrocarbons (PAHs) have a negative impact on human health due to their mutagenic and/or carcinogenic properties, the objective of this work was to study the influence of tobacco smoke on levels and phase distribution of PAHs and to evaluate the associated health risks. The air samples were collected at two homes; 18 PAHs (the 16 PAHs considered by U.S. EPA as priority pollutants, dibenzo[a,l]pyrene and benzo[j]fluoranthene) were determined in gas phase and associated with thoracic (PM10) and respirable (PM2.5) particles. At home influenced by tobacco smoke the total concentrations of 18 PAHs in air ranged from 28.3 to 106 ngm 3 (mean of 66.7 25.4 ngm 3),∑PAHs being 95% higher than at the non-smoking one where the values ranged from 17.9 to 62.0 ngm 3 (mean of 34.5 16.5 ngm 3). On average 74% and 78% of ∑PAHs were present in gas phase at the smoking and non-smoking homes, respectively, demonstrating that adequate assessment of PAHs in air requires evaluation of PAHs in both gas and particulate phases. When influenced by tobacco smoke the health risks values were 3.5e3.6 times higher due to the exposure of PM10. The values of lifetime lung cancer risks were 4.1 10 3 and 1.7 10 3 for the smoking and nonsmoking homes, considerably exceeding the health-based guideline level at both homes also due to the contribution of outdoor traffic emissions. The results showed that evaluation of benzo[a]pyrene alone would probably underestimate the carcinogenic potential of the studied PAH mixtures; in total ten carcinogenic PAHs represented 36% and 32% of the gaseous ∑PAHs and in particulate phase they accounted for 75% and 71% of ∑PAHs at the smoking and non-smoking homes, respectively.

Polycyclic aromatic hydrocarbons: levels and phase distributions in preschool microenvironment

This work aims to characterize levels and phase distribution of polycyclic aromatic hydrocarbons (PAHs) in indoor air of preschool environment and to assess the impact of outdoor PAH emissions to indoor environment. Gaseous and particulate (PM1 and PM2.5) PAHs (16 USEPA priority pollutants, plus dibenzo[a,l]pyrene, and benzo[j]fluoranthene) were concurrently sampled indoors and outdoors in one urban preschool located in north of Portugal for 35 days. The total concentration of 18 PAHs (ΣPAHs) in indoor air ranged from 19.5 to 82.0 ng/m3; gaseous compounds (range of 14.1–66.1 ng/m3) accounted for 85% ΣPAHs. Particulate PAHs (range 0.7–15.9 ng/m3) were predominantly associated with PM1 (76% particulate ΣPAHs) with 5-ring PAHs being the most abundant. Mean indoor/outdoor ratios (I/O) of individual PAHs indicated that outdoor emissions significantly contributed to PAH indoors; emissions from motor vehicles and fuel burning were the major sources.

Hydrogen sulfide measurement by headspace-gas chromatography-mass spectrometry (HS-GC-MS): application to gaseous samples and gas dissolved in muscle.

The aim of our study was to present a new headspace-gas chromatography-mass spectrometry (HS-GC-MS) method applicable to the routine determination of hydrogen sulfide (H(2)S) concentrations in biological and gaseous samples. The primary analytical drawback of the GC/MS methods for H(2)S measurement discussed in the literature was the absence of a specific H(2)S internal standard required to perform quantification. Although a deuterated hydrogen sulfide (D(2)S) standard is currently available, this standard is not often used because this standard is expensive and is only available in the gas phase. As an alternative approach, D(2)S can be generated in situ by reacting deuterated chloride with sodium sulfide; however, this technique can lead to low recovery yield and potential isotopic fractionation. Therefore, N(2)O was chosen for use as an internal standard. This method allows precise measurements of H(2)S concentrations in biological and gaseous samples. Therefore, a full validation using accuracy profile based on the β-expectation tolerance interval is presented. Finally, this method was applied to quantify H(2)S in an actual case of H(2)S fatal intoxication.

Gas-phase solvolysis type reactions of SiCl3+ cations

Gas-phase SiCl3+ ions undergo sequential solvolysis type reactions with water, methanol, ammonia, methylamine and propylene. Studies carried out in a Fourier Transform mass spectrometer reveal that these reactions are facile at 10-8 Torr and give rise to substituted chlorosilyl cations. Ab initio and DFT calculations reveal that these reactions proceed by addition of the silyl cation to the oxygen or nitrogen lone pair followed by a 1,3-H migration in the transition state. These transition states are calculated to lie below the energy of the reactants. By comparison, hydrolysis of gaseous CCl3+ is calculated to involve a substantial positive energy barrier.