92 resultados para isopropanol


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Abstract Background Due to the growing number of outbreaks of infection in hospital nurseries, it becomes essential to set up a sanitation program that indicates that the appropriate chemical agent was chosen for application in the most effective way. Method For the purpose of evaluating the efficacy of a chemical agent, the minimum inhibitory concentration (MIC) was reached by the classic method of successive broth dilutions. The reference bacteria utilized were Bacillus subtilis var. globigii ATCC 9372, Bacillus stearothermophilus ATCC 7953, Escherichia coli ATCC 25922, Staphylococcus aureus ATCC 25923. The strains of Enterobacter cloacae IAL 1976 (Adolfo Lutz Institute), Serratia marcescens IAL 1478 and Acinetobactev calcoaceticus IAL 124 (ATCC 19606), were isolated from material collected from babies involved in outbreaks of infection in hospital nurseries. Results The MIC intervals, which reduced bacteria populations over 08 log10, were: 59 to 156 mg/L of quaternarium ammonium compounds (QACs); 63 to 10000 mg/L of chlorhexidine digluconate; 1375 to 3250 mg/L of glutaraldehyde; 39 to 246 mg/L of formaldehyde; 43750 to 87500 mg/L of isopropanol or ethanol; 1250 to 6250 mg/L of iodine in polyvinyl-pyrolidone complexes, 150 to 4491 mg/L of chlorine-releasing-agents (CRAs); 469 to 2500 mg/L of hydrogen peroxide; and, 2310 to 18500 mg/L of peracetic acid. Conclusions Chlorhexidine showed non inhibitory activity over germinating spores. A. calcoaceticus, was observed to show resistance to the majority of the agents tested, followed by E. cloacae and S. marcescens.

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Biohybrid derivatives of π-conjugated materials are emerging as powerful tools to study biological events through the (opto)electronic variations of the π-conjugated moieties, as well as to direct and govern the self-assembly properties of the organic materials through the organization principles of the bio component. So far, very few examples of thiophene-based biohybrids have been reported. The aim of this Ph. D thesis has been the development of oligothiophene-oligonucleotide hybrid derivatives as tools, on one side, to detect DNA hybridisation events and, on the other, as model compounds to investigate thiophene-nucleobase interactions in the solid state. To obtain oligothiophene bioconjugates with the required high level of purity, we first developed new synthetic ecofriendly protocols for the synthesis of thiophene oligomers. Our innovative heterogeneous Suzuki coupling methodology, carried out in EtOH/water or isopropanol under microwave irradiation, allowed us to obtain alkyl substituted oligothiophenes and thiophene based co-oligomers in high yields and very short reaction times, free from residual metals and with improved film forming properties. These methodologies were subsequently applied in the synthesis of oligothiophene-oligonucleotide conjugates. Oligothiophene-5-labeled deoxyuridines were synthesized and incorporated into 19-meric oligonucletide sequences. We showed that the oligothiophene-labeled oligonucletide sequences obtained can be used as probes to detect a single nucleotide polymorphism (SNP) in complementary DNA target sequences. In fact, all the probes showed marked variations in emission intensity upon hybridization with a complementary target sequence. The observed variations in emitted light were comparable or even superior to those reported in similar studies, showing that the biohybrids can potentially be useful to develop biosensors for the detection of DNA mismatches. Finally, water-soluble, photoluminescent and electroactive dinucleotide-hybrid derivatives of quaterthiophene and quinquethiophene were synthesized. By means of a combination of spectroscopy and microscopy techniques, electrical characterizations, microfluidic measurements and theoretical calculations, we were able to demonstrate that the self-assembly modalities of the biohybrids in thin films are driven by the interplay of intra and intermolecular interactions in which the π-stacking between the oligothiophene and nucleotide bases plays a major role.

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CZE coupled to sheath liquid-based electrospray ionization (ESI) and multiple-stage ion trap mass spectrometry (MS(n) ) was used for the confirmation analysis of ethyl glucuronide (EtG) and ethyl sulfate (EtS) in human serum and urine collected after intake of alcoholic beverages. Electrophoretic separations were performed in uncoated fused-silica capillaries using a pH 9.5 ammonium acetate background electrolyte and normal polarity. MS detection of EtG and EtS occurred after negative ionization using a spray liquid containing 0.5% v/v ammonia in isopropanol/water (60:40%, v/v). CZE-MS and CZE-MS² results obtained after injection of solid-phase extracts for EtG and EtS and of diluted urine confirmed the presence of EtG and EtS in samples whose levels were previously determined by CZE with indirect UV detection. Detection limits of each compound were estimated to be around 2.0 (injection of diluted urine) and 0.2 μg/mL (extracts).

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Supercritical carbon dioxide is used to exfoliate graphite, producing a small, several-layer graphitic flake. The supercritical conditions of 2000, 2500, and 3000 psi and temperatures of 40°, 50°, and 60°C, have been used to study the effect of critical density on the sizes and zeta potentials of the treated flakes. Photon Correlation Spectroscopy (PCS), Brunauer-Emmett-Teller (BET) surface area measurement, field emission scanning electron microscopy (FE-SEM), and atomic force microscopy (AFM) are used to observe the features of the flakes. N-methyl-2-pyrrolidinone (NMP), dimethylformamide (DMF), and isopropanol are used as co-solvents to enhance the supercritical carbon dioxide treatment. As a result, the PCS results show that the flakes obtained from high critical density treatment (low temperature and high pressure) are more stable due to more negative charges of zeta potential, but have smaller sizes than those from low critical density (high temperature and low pressure). However, when an additional 1-hour sonication is applied, the size of the flakes from low critical density treatment becomes smaller than those from high critical density treatment. This is probably due to more CO2 molecules stacked between the layers of the graphitic flakes. The zeta potentials of the sonicated samples were slightly more negative than nonsonicated samples. NMP and DMF co-solvents maintain stability and prevented reaggregation of the flakes better than isopropanol. The flakes tend to be larger and more stable as the treatment time increases since larger flat area of graphite is exfoliated. In these experiments, the temperature has more impact on the flakes than pressure. The BET surface area resultsshow that CO2 penetrates the graphite layers more than N2. Moreover, the negative surface area of the treated graphite indicates that the CO2 molecules may be adsorbed between the graphite layers during supercritical treatment. The FE-SEM and AFM images show that the flakes have various shapes and sizes. The effects of surfactants can be observed on the FE-SEM images of the samples in one percent by weight solution of SDBS in water since the sodium dodecylbenzene sulfonate (SDBS) residue covers all of the remaining flakes. The AFM images show that the vertical thickness of the graphitic flakes can ranges from several nanometers (less than ten layers thick), to more than a hundred nanometers. In conclusion, supercritical carbon dioxide treatment is a promising step compared to mechanical and chemical exfoliation techniques in the large scale production of thin graphitic flake, breaking down the graphite flakes into flakes only a fewer graphene layers thick.

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There is increasing evidence for an additional acute, nongenomic action of the mineralocorticoid hormone aldosterone on renal epithelial cells, leading to a two-step model of mineralocorticoid action on electrolyte excretion. We investigated the acute effect of aldosterone on intracellular free Ca2+ and on intracellular pH in an aldosterone-sensitive Madin-Darby canine kidney cell clone. Within seconds of application of aldosterone, but not of the glucocorticoid hydrocortisone, there was a 3-fold sustained increase of intracellular Ca2+ at a half-maximal concentration of 10(-10) mol/liter. Omission of extracellular Ca2+ prevented this hormone response. In the presence of extracellular Ca2+ aldosterone led to intracellular alkalinization. The Na+/H+ exchange inhibitor ethyl-isopropanol-amiloride (EIPA) prevented the aldosterone-induced alkalinization but not the aldosterone-induced increase of intracellular Ca2+. Omission of extracellular Ca2+ also prevented aldosterone-induced alkalinization. Instead, aldosterone led to a Zn(2+)-dependent intracellular acidification in the presence of EIPA, indicative of an increase of plasma membrane proton conductance. Under control conditions, Zn2+ prevented the aldosterone-induced alkalinization completely. We conclude that aldosterone stimulated net-entry of Ca2+ from the extracellular compartment and a plasma membrane H+ conductance as prerequisites for the stimulation of plasma membrane Na+/H+ exchange which in turn modulates K+ channel acitivity. It is probable that the aldosterone-sensitive H+ conductance maintains Na+/H+ exchange activity by providing an acidic environment in the vicinity of the exchanger. Thus, genomic action of aldosterone determines cellular transport equipment, whereas the nongenomic action regulates transporter activity that requires responses within seconds or minutes, which explains the rapid effects on electrolyte excretion.

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The crystal structure of the xanthine oxidase-related molybdenum-iron protein aldehyde oxido-reductase from the sulfate reducing anaerobic Gram-negative bacterium Desulfovibrio gigas (Mop) was analyzed in its desulfo-, sulfo-, oxidized, reduced, and alcohol-bound forms at 1.8-A resolution. In the sulfo-form the molybdenum molybdopterin cytosine dinucleotide cofactor has a dithiolene-bound fac-[Mo, = O, = S, ---(OH2)] substructure. Bound inhibitory isopropanol in the inner compartment of the substrate binding tunnel is a model for the Michaelis complex of the reaction with aldehydes (H-C = O,-R). The reaction is proposed to proceed by transfer of the molybdenum-bound water molecule as OH- after proton transfer to Glu-869 to the carbonyl carbon of the substrate in concert with hydride transfer to the sulfido group to generate [MoIV, = O, -SH, ---(O-C = O, -R)). Dissociation of the carboxylic acid product may be facilitated by transient binding of Glu-869 to the molybdenum. The metal-bound water is replenished from a chain of internal water molecules. A second alcohol binding site in the spacious outer compartment may cause the strong substrate inhibition observed. This compartment is the putative binding site of large inhibitors of xanthine oxidase.

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O principal resíduo da indústria de café solúvel é a borra de café, gerada após a extração de sólidos solúveis com água, sendo usualmente queimada em caldeiras para geração de energia para a própria indústria. Entretanto, este co-produto pode conter de 15 a 20 % de óleo, componente de grande interesse na indústria alimentícia. Em paralelo, na indústria de produção de óleos vegetais o solvente frequentemente utilizado é o hexano. Contudo, por este ser um derivado de combustíveis fósseis, alternativas para sua substituição por solventes mais amigáveis ao meio ambiente, que podem ser obtidos por via biotecnológica, estão sendo estudadas. Deste modo, o objetivo principal desta dissertação de mestrado foi a viabilização técnica do emprego de solventes alcoólicos no processo de extração de óleo de borra de café proveniente da indústria de processamento de café solúvel. Foram realizadas extrações sólido-líquido em um estágio para estudar a influência das variáveis de processo temperatura (60 a 90 °C), tipo de solvente (etanol, ET ou isopropanol, IPA) e a hidratação do solvente (absoluto ou azeotrópico) nas características das fases extrato e rafinado, em termos de rendimento de extração de óleo, de ácidos clorogênicos (ACG), de carboidratos totais, teor de proteínas e índice de solubilidade de nitrogênio (ISN) da fase rafinado. Pré-tratamento enzimático ao processo de extração também foi realizado para investigar a sua atuação sobre o rendimento de extração de óleo e ACG, além do ISN das fases rafinado obtidas na temperatura de 70 °C. De forma geral, pode-se inferir que a temperatura favorece a extração de compostos lipídicos, mas a hidratação do solvente prejudica a extração destes compostos pelo aumento da polaridade do solvente. Do mesmo modo, como o ET é mais polar que o IPA, o primeiro solvente proporcionou a obtenção de menores rendimentos de extração de óleo. A temperatura de processo também influenciou a extração de ACG, a qual foi beneficiada a temperaturas mais baixas pelo aumento da polaridade dos solventes utilizados. De tal forma, que a 60 °C, nos experimentos utilizando etanol azeotrópico obteve-se os menores rendimentos de extração de óleo, porém maior rendimento de extração de ACG. O pré-tratamento enzimático apresentou diferenças significativas nas características das fases extrato e rafinado. No entanto, somente os experimentos com etanol absoluto resultaram em rendimentos de extração de óleo economicamente viáveis. De fato, será relevante um estudo mais aprofundado das variáveis de pré-tratamento enzimático para obter resultados mais expressivos em relação à extração de compostos lipídicos. Diante dos dados experimentais obtidos, conclui-se que é tecnicamente viável o emprego de solventes alcoólicos no processo de extração de óleo de borra de café. Entretanto, nota-se que as condições de processo devem ser avaliadas minuciosamente com o objetivo de se obter altos rendimentos de extração de óleo com maior teor de ACG.

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Este trabalho teve como principal objetivo produzir membranas porosas de carboximetilquitosana e hidrogéis de quitosana com propriedades físico-químicas e mecânicas adequadas para aplicações em Engenharia de Tecidos. Para isso, quitosanas com diferentes graus de acetilação (4,0%<GA<40%) e de elevada massa molar média viscosimétrica (Mv>750.000 g.mol-1) foram produzidas através da aplicação de processos consecutivos de desacetilação assistida por irradiação de ultrassom de alta intensidade (DAIUS) à beta-quitina extraída de gládios de lulas Doryteuthis spp. A carboximetilação de quitosana extensivamente desacetilada (Qs-3; GA=4%) foi realizada pela reação com ácido monocloroacético em meio isopropanol/solução aquosa de NaOH, gerando a amostra CMQs-0 (GS≈0,98; Mv≈190.000 g.mol-1). A irradiação de ultrassom de alta intensidade foi empregada para tratar solução aquosa de CMQs-0 durante 1 h e 3 h, resultando nas amostras CMQs-1 (Mv≈94.000 g.mol-1) e CMQs-3 (Mv≈43.000 g.mol-1), respectivamente. Para a produção de membranas reticuladas, genipina foi adicionada em diferentes concentrações (1,0x10-4 mol.L-1, 3,0x10-4 mol.L-1 ou 5,0x10-4 mol.L-1) às soluções aquosas das CMQs, que foram vertidas em placas de Petri e a reação de reticulação procedeu por 24 h. Em seguida, as membranas reticuladas (M-CMQs) foram liofilizadas, neutralizadas, lavadas e liofilizadas novamente, resultando em nove amostras, que foram caracterizadas quanto ao grau médio de reticulação (GR), grau médio de hidratação (GH), morfologia, propriedades mecânicas e quanto à susceptibilidade à degradação por lisozima. O grau médio de reticulação (GR) foi tanto maior quanto maior a concentração de genipina empregada na reação, variando de GR≈3,3% (M-CMQs-01) a GR≈17,8% (M-CMQs-35). As análises de MEV revelaram que as membranas reticuladas M-CMQs são estruturas porosas que apresentam maior densidade de poros aparentes quanto maiores os valores de Mve GR. Entretanto, as membranas preparadas a partir de CMQs de elevada massa molar (Mv>94.000 g.mol-1) e pouco reticuladas (GR<10%), apresentaram propriedades mecânicas superiores em termos de resistência máxima à tração (>170 kPa) e elongação máxima à ruptura (>40%). Por outro lado, as membranas mais susceptíveis à degradação enzimática foram aquelas preparadas a partir de CMQs de baixa massa molar (Mv≈43.000 g.mol-1) e que exibiram baixos graus de reticulação (GR<11%). Hidrogéis estáveis de quitosana sem o uso de qualquer agente de reticulação externo foram produzidos a partir da gelificação de soluções aquosas de quitosana com solução de NaOH ou vapor de NH3. Os hidrogéis produzidos a partir de soluções de quitosana de elevada massa molar média ponderal (Mw≈640.000 g.mol-1) e extensivamente desacetilada (DA≈2,8%) em concentrações poliméricas acima 2,0%, exibiram melhores propriedades mecânicas com o aumento da concentração polimérica, devido à formação de numerosos emaranhamentos físicos das cadeias poliméricas em solução. Os resultados mostram que as propriedades físico-químicas e mecânicas dos hidrogéis de quitosana podem ser controladas variando a concentração do polímero e o processo de gelificação. A avaliação biológica de tais hidrogéis para a regeneração de miocárdio infartado de ratos revelou que os hidrogéis de quitosana preparados a partir de soluções de polímero a 1,5% foram perfeitamente incorporados sobre a superfície do epicárdio do coração e apresentaram degradação parcial acompanhada por infiltração de células mononucleares.

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In the present study, nanocrystalline titanium dioxide (TiO2) was prepared by sol–gel method at low temperature from titanium tetraisopropoxide (TTIP) and characterized by different techniques (gas adsorption, XRD, TEM and FTIR). Variables of the synthesis, such as the hydrolyzing agent (acetic acid or isopropanol) and calcination temperatures (300–800 °C), were analyzed to get uniform size TiO2 nanoparticles. The effect that these two variables have on the structure of the resultant TiO2 nanoparticles and on their photocatalytic activity is investigated. The photocatalytic activities of TiO2 nanoparticles were evaluated for propene oxidation at low concentration (100 ppmv) under two different kinds of UV light (UV-A ∼ 365 nm and UV-C ∼ 257.7 nm) and compared with Degussa TiO2 P-25, used as reference sample. The results show that both hydrolyzing agents allow to prepare TiO2 nanoparticles and that the hydrolyzing agent influences the crystalline structure and its change with the thermal treatments. Interestingly, the prepared TiO2 nanoparticles possess anatase phase with small crystalline size, high surface area and higher photocatalytic activity for propene oxidation than commercial TiO2 (Degussa P-25) under UV-light. Curiously, these prepared TiO2 nanoparticles are more active with the 365 nm source than with the 257.7 nm UV-light, which is a remarkable advantage from an application point of view. Additionally, the obtained results are particularly good when acetic acid is the hydrolyzing agent at both wavelengths used, possibly due to the high crystallinity, low anatase phase size and high surface oxygen groups’ content in the nanoparticles prepared with it, in comparison to those prepared using isopropanol.

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The objective of this research was to investigate the oxidation of organic compounds in molten alkali metal hydroxides containing manganates. It has been shown that controlled oxidation can be readily achieved with high specificity to give products in high yield with very short reaction times. The concurrent changes in the melt were monitored using a vibrating platinum indicator electrode with a quazi-reference electrode which was successfully developed for use in molten (Na-K)OH eutectic at 523K. Henry's Law constants for water in the molten eutectic system (Na-K)OH have been measured and used to calculate the water concentration in the melt. The electrochemistry of manganates in molten (Na-K)OH eutectic at 523K has been studied using the vibrating platinum electrode, and the existence of the species Mn(II), Mn(II!), Mn(IV), Mn(V) and Mn(VI) in such melts has been investigated at various water concentrations. The half-wave potentials of the voltammetric waves were measured versus the cathodic limit of the melt. The stability of Mn(V) or Mn(VI) in the melt was achieved by varying the water concentration. A range of organic chemicals has been passed through molten (Na-K)OH at 523K and the reactions of these chemicals with the melt have been studied. The same organics were then passed through molten (Na-K)OH containing stabilized Mn(V) or Mn{VI) without violent reaction. Methanol, allyl alcohol, propane 1, 2 diol, I-heptene and acetone were oxidized by Mn(V) and Mn(VI). Ethanol was only oxidized by Mn(VI), isopropanol and benzyl alcohol were only oxidized by Mn(V). Npropanol, butanol, 2 methyl propan-2-ol, n-hexane, n-heptane toluene and cyclohexane were unchanged by both Mn(V) and Mn(VI). Detailed experiments have been performed on the reactions of ethanol, iso-propanol and methanol in molten (Na-K)OH containing stabilized Mrt(V) or Mn(VI), and reaction mechanisms have been postulated. Ethanol and iso-propanol were oxidized to acetaldehyde and acetone respectively with a potential for useful chemical process. The oxidation of methanol could be developed as a basis for an industrial methanol disposal process.

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Once familiar with the fire test rig constructed by M Kay, and modified to allow incorporation of both video and computer facilities, Melamine Phosphate production was scaled up from small to large laboratory scale, and then commercial scale production was considered. Samples produced at each stage were compared analytically, visually and in fire testing. The separation and drying stages on a commercial scale lay unresolved practically, due to lack of test facilities. Different cure regimes for the Araldite MY753 and Versamid system were investigated along with weathering tests and cured samples. Surface priming is suggested for large scale application, though on a small scale a clean unprimed surface was thought sufficient. Some samples heat, aired, cracked at the edges but remained bonded on fire testing. An intumescent sample containing Melamine Phosphate, Araldite and Versamid could not be applied to a vertical surface successfully, the viscosity had to be increased to allow application and curing, various additives were tested, two successful ones being fumed silica and a solvent, isopropanol. The low percentages fumed silica used was incorporated into the sample and the viscosity and fire test results compared with a `standard sample'. An expanding graphite incorporated into a standard sample made mixing and application increasingly difficult, due to the lubricating affect of graphite, but the char produced was a good quality, stable char. A suitable formulation could now be mixed, applied and cured, and assuming no adverse interaction between the additives would protect the sample in the event of a fire.

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The literature relating to evaporation from single droplets of pure liquids and the drying of solution and slurry droplets, and of droplet sprays has been reviewed. The heat and mass transfer rates for individual droplets suspended in free-flight, were investigated using a specially-designed vertical wind tunnel, to simulate conditions in a spray drier. The technique represented a unique alternative method for investigating evaporation from unrestrained single droplets with variable residence times. The experiments covered droplets of pure liquid allowbreak (water, isopropanol) allowbreak and of significantly different solutions (sucrose, potassium sulphate) over a range of temperatures of 37oC to 97oC, initial concentrations of 5 to 40wt/wt% , and initial drop sizes of 2.8 to 4.6mm. Drop behaviour was recorded photographically and dried particles were examined by Scanning Electron Microscopy. Correlations were developed for mass transfer coefficients for pure water droplets in free-flight; (i) experiencing oscillations, rotation and deformation, Sh = -105 + 3.9 [Ta - Td/Tamb]0.18Re0.5Sc033 for Re approx. > 1380 (ii) when these movements had ceased or diminished, Sh = 2.0 + 0.71 [Ta - Td/Tamb]0.18Re0.5Sc033 for Re approx. < 1060. Data for isopropanol drops were correlated resonably well by these equations. The heat transfer data showed a similar transition range. The drying rate curves for drops of sucrose and potassium sulphate solution exhibited three distinct stages; an initial increase in the drying rate as drop temperature reduced to the wet-bulb temperature, a short constant-rate period and a falling-rate period characterised by formation of a crust which controlled the mass transfer rate. Due to drop perturbation the rates in the high Re number region were up to 5 times greater than predicted from theory for spherical droplets. In the case of sucrose solution a `skin' formed over the drop surface prior to crust formation. This provided an additional resistance to mass transfer and resulted in extended drying times and a smooth crust of low porosity. The relevance of the results to practical spray drying operations is discussed.

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Lipidome profile of fluids and tissues is a growing field as the role of lipids as signaling molecules is increasingly understood, relying on an effective and representative extraction of the lipids present. A number of solvent systems suitable for lipid extraction are commonly in use, though no comprehensive investigation of their effectiveness across multiple lipid classes has been carried out. To address this, human LDL from normolipidemic volunteers was used to evaluate five different solvent extraction protocols [Folch, Bligh and Dyer, acidified Bligh and Dyer, methanol (MeOH)-tert-butyl methyl ether (TBME), and hexane-isopropanol] and the extracted lipids were analyzed by LC-MS in a high-resolution instrument equipped with polarity switching. Overall, more than 350 different lipid species from 19 lipid subclasses were identified. Solvent composition had a small effect on the extraction of predominant lipid classes (triacylglycerides, cholesterol esters, and phosphatidylcholines). In contrast, extraction of less abundant lipids (phosphatidylinositols, lyso-lipids, ceramides, and cholesterol sulfates) was greatly influenced by the solvent system used. Overall, the Folch method was most effective for the extraction of a broad range of lipid classes in LDL, although the hexane-isopropanol method was best for apolar lipids and the MeOH-TBME method was suitable for lactosyl ceramides. Copyright © 2013 by the American Society for Biochemistry and Molecular Biology, Inc.

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The Intoxilyzer 5000 was tested for calibration curve linearity for ethanol vapor concentration between 0.020 and 0.400g/210L with excellent linearity. Calibration error using reference solutions outside of the allowed concentration range, response to the same ethanol reference solution at different temperatures between 34 and 38$\sp\circ$C, and its response to eleven chemicals, 10 mixtures of two at the time, and one mixture of four chemicals potentially found in human breath have been evaluated. Potential interferents were chosen on the basis of their infrared signatures and the concentration range of solutions corresponding to the non-lethal blood concentration range of various volatile organic compounds reported in the literature. The result of this study indicates that the instrument calibrates with solutions outside the allowed range up to $\pm$10% of target value. Headspace FID dual column GC analysis was used to confirm the concentrations of the solutions. Increasing the temperature of the reference solution from 34 to 38$\sp\circ$C resulted in linear increases in instrument recorded ethanol readings with an average increase of 6.25%/$\sp\circ$C. Of the eleven chemicals studied during this experiment, six, isopropanol, toluene, methyl ethyl ketone, trichloroethylene, acetaldehyde, and methanol could reasonably interfere with the test at non-lethal reported blood concentration ranges, the mixtures of those six chemicals showed linear additive results with a combined effect of as much as a 0.080g/210L reading (Florida's legal limit) without any ethanol present. ^

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Azulenyl nitrone (AZN) is a bright green compound that can be used to stain different compounds, including plastics. When these stained plastics are irradiated, as they commonly are in the sterilization of medical devices, AZN changes color from green to red, constituting a permanent change. This would make obsolete the current methods of radioactive labeling and maintain the integrity of medical equipment. Although a method of synthesis is already in place, the aim was to improve the yield significantly and find a more efficient and cost-effective procedure. Last year, the procedure used resulted in 18 to 20% of AZN synthesized at the most favorable conditions. With that in mind, this year modifications were done in the hopes of improving the yield. The solvent was changed to a mixture of isopropanol and triethylamine, a stronger base, and a catalytic amount of N-tertbutyl hydroxylamine hydrochloride was used (around 4 equivalents). The reaction time was also increased to 7 days, rather than 2. After several trials, the samples were run through column chromatography and the average yield was 70%, a much more promising result than that obtained last year. There is still research to be done to improve the technicalities of the procedure, including altering the amounts of N-tertbutyl hydroxylamine hydrochloride to try and obtain similar data with fewer amounts. This portion of the research will be done in the second half of the year. In the meantime, however, a novel and more efficient method of synthesis has been established for the production of AZN that can be potentially commercialized.