Conductivity sensor technology application in steady state migration test

In this paper the current development of the steady state migration test was reviewed. Experiments were carried out for a series of concrete mixes with the steady state migration test in which conductivity sensor technology is applied. With the developed steady state migration test, conductivity in anolyte, loop current and temperature can be monitored in real time. The experimental results are conductive to understand the mechanism of chloride migration during both unsteady state and steady state. The conductivity of anolyte could be used to calculate the chloride concentration in anolyte and the theoretical correlation between them was explained. Over all, the developed steady state migration is an effective, convenient, well-defined in theory and plentiful with information method which could be used to determine the chloride diffusion coefficient of cementitious materials.

Extracção supercrítica de óleo de grainha de uva combinada com pré-tratamentos enzimáticos

Neste trabalho estudou-se a extracção supercrítica do óleo de grainha de uva, usando dióxido de carbono, e combinou-se este processo com um prétratamento enzimático da semente para aumentar o rendimento global da extracção. A qualidade dos extractos obtidos foi avaliada pelo seu conteúdo em triacilglicerídeos, perfil de ácidos gordos e capacidade antioxidante. Realizaram-se também alguns estudos exploratórios sobre a aplicação de um pré-tratamento de alta pressão (HPP) à grainha da uva. Adicionalmente, efectuou-se o estudo da extracção, fraccionamento e caracterização estrutural das procianidinas da grainha da uva, bem como a avaliação da sua capacidade antioxidante. A extracção de procianidinas da grainha da uva foi efectuada sequencialmente com metanol e acetona/água, tendo sido posteriormente fraccionadas por adição sucessiva de misturas metanol/clorofórmio progressivamente mais concentradas em clorofórmio. A caracterização das procianidinas foi feita por HPLC-UV e LC–MS, antes e depois de sujeitar as amostras a uma tiólise, e também por ESI-MS e ESI-MS/MS. Este estudo permitiu reportar, pela primeira vez, a ocorrência de procianidinas do tipo-A galoiladas na grainha da uva. Os resultados de HPLC-UV permitiram determinar o grau médio de polimerização das procianidinas e a sua composição monomérica em (+)- catequina, (-)-epicatequina e (-)-epicatequina-O-galato. Mostrou-se que a (+)- catequina é o flavan-3-ol terminal mais abundante e a (-)-epicatequina predomina largamente como unidade de extensão. No caso de procianidinas do tipo A, a ligação interflavânica C2-C7 encontra-se essencialmente nas unidades terminais. O grau médio de polimerização das diversas fracções varia entre 1.0 e 10.8. A sua capacidade antioxidante, medida pelo método espectrofotométrico de DPPH•, mostrou-se ser equivalente à de uma amostra comercial de (+)-catequina usada como referência. A partir dos graus médios de polimerização experimentais e das análises de FTIR das fracções correspondentes foi possível obter um modelo preditivo O-PLS com apenas uma variável latente. O pré-tratamento enzimático justificou-se pelo conhecimento existente acerca do uso de enzimas específicas que destroem parcialmente as paredes celulares. Atendendo à composição das paredes celulares da grainha da uva preparou-se uma suspensão contendo protease, xilanase, pectinase e celulase. Para determinar as condições experimentais do pré-tratamento que maximizam o rendimento da extracção, estudou-se o efeito do tempo de reacção, temperatura, pH, diâmetro médio das partículas de grainha moída e a concentração das enzimas. Os incrementos do rendimento da extracção de óleo observados atingiram 163.2%. O estudo da extracção supercrítica (SFE) do óleo da grainha de uva tratada e não-tratada permitiu obter as curvas de extracção correspondentes, bem com analisar a influência das condições operatórias sobre o seu andamento. Montou-se uma instalação laboratorial onde se realizaram experiências com dióxido de carbono a 160, 180, 200 e 220 bar e temperaturas de 313.15 e 323.15 K. Os rendimentos obtidos por SFE foram semelhantes aos de Soxhlet com n-hexano. As curvas de extracção medidas compreendem um primeiro período de extracção, onde se remove cerca de 92-97% do óleo disponível, e um segundo período, essencialmente difusional, com pouco impacto no rendimento final. Os vários extractos recolhidos e o óleo global obtido foram caracterizados para avaliar a sua qualidade e relacioná-la com as condições operatórias de SFE. Determinaram-se o conteúdo total em triacilglicerídeos, o seu perfil de ácidos gordos e a capacidade antioxidante (AOC). Os resultados mostraram que a AOC aumenta com a elevação da pressão e, acentuadamente, com o acréscimo da temperatura. Ao longo da curva de extracção, a AOC é mais pronunciada nos extractos iniciais, nomeadamente nos primeiros 30 a 40% da extracção. A modelação efectuada considerou que o óleo extractável se reparte entre células rompidas, predominantes na periferia da semente, e células intactas, mais interiores. Admitiu-se que o transporte de massa ocorre em série, i.e. das células intactas para as rompidas e destas para o solvente; mostrou-se que a dispersão axial era desprezável. Os balanços materiais à fase fluida e aos volumes de células rompidas e intactas, combinados com os fluxos interno, externo e a relação de equilíbrio foram resolvidos numericamente pelo método das linhas combinado com diferenças finitas atrasadas. O modelo reproduziu bem as curvas experimentais e permitiu simular curvas de eluição e os três perfis de concentração no leito.

Synaptic dysfunction in early encephalopathies : from genes to function

Tese de doutoramento, Medicina (Neurologia), Universidade de Lisboa, Faculdade de Medicina, 2015

Desenvolvimento de métodos de análise físico-química em águas usando um analisador multiparamétrico AQUAKEM

Trabalho Final de mestrado para obtenção do grau de Mestre em Engenharia Química e Biológica

Expression des cotransporteurs cation-chlorure KCC2 et NKCC1 au cours du développement de la moelle épinière de l’opossum Monodelphis domestica

L’inhibition est nécessaire à la génération d’outputs coordonnés entre muscles antagonistes lors de la locomotion. Une baisse de la concentration neuronale en ions chlorure au cours du développement des mammifères conduit à l’émergence de l’inhibition. Cette baisse repose sur l’équilibre entre deux cotransporteurs cation-chlorure, KCC2 et NKCC1. KCC2 expulse Cl- de la cellule alors que NKCC1 pompe Cl- dans la cellule. L’opossum Monodelphis domestica naît dans un état très immature. Le seul comportement locomoteur qu’il présente à la naissance consiste en des mouvements rythmiques et alternés des membres antérieurs pour grimper le long du ventre de la mère vers une tétine. Les membres postérieurs sont des bourgeons immobiles dont le développement est en grande partie postnatal. Pour cette raison, cette espèce constitue un modèle idéal pour l’étude du développement locomoteur. Afin d’étudier les mécanismes conduisant à l’émergence de l’inhibition durant le développement moteur, nous avons décrit l’expression développementale de KCC2 et NKCC1 chez l’opossum postnatal par immunohistochimie au niveau des renflements spinaux. Les motoneurones et afférences primaires ont été identifiés en utilisant un marquage rétrograde au TRDA. Le marquage pour KCC2 et NKCC1 est détecté dans la moelle épinière ventrale dans la matière grise et blanche présomptive dès la naissance, ce qui suggère que l’inhibition serait déjà mise en place avant la naissance, permettant subséquemment l’alternance des membres antérieurs observée chez les nouveau-nés. L’expression développementale de KCC2 et NKCC1 suit des gradients ventrodorsal et médiolatéral, tels qu’observés chez les rongeurs (rats et souris). Le patron mature d’expression de ces cotransporteurs est observé aux alentours de la 5ème semaine postnatale lorsque la locomotion de l’opossum est mature. Enfin, entre la naissance et P5, les dendrites exprimant KCC2 au niveau de la corne dorsale sont retrouvées en apposition aux afférences primaires ce qui suggère un rôle de KCC2 dans la formation des circuits sensori-moteurs.

Caractérisation de la pharmacocinétique de formulations sensibles au pH et de formulations destinées au traitement des intoxications médicamenteuses

La préparation de formulations à libération contrôlée est le domaine des sciences pharmaceutiques qui vise à modifier l’environnement immédiat des principes actifs pour en améliorer l’efficacité et l’innocuité. Cet objectif peut être atteint en modifiant la cinétique de circulation dans le sang ou la distribution dans l’organisme. Le but de ce projet de recherche était d’étudier le profil pharmacocinétique (PK) de différentes formulations liposomales. L’analyse PK, généralement employée pour représenter et prédire les concentrations plasmatiques des médicaments et de leurs métabolites, a été utilisée ici pour caractériser in vivo des formulations sensibles au pH servant à modifier la distribution intracellulaire de principes actifs ainsi que des liposomes destinés au traitement des intoxications médicamenteuses. Dans un premier temps, la PK d’un copolymère sensible au pH, à base de N-isopropylacrylamide (NIPAM) et d’acide méthacrylique (MAA) a été étudiée. Ce dernier, le p(NIPAM-co-MAA) est utilisé dans notre laboratoire pour la fabrication de liposomes sensibles au pH. L’étude de PK conduite sur les profils de concentrations sanguines de différents polymères a défini les caractéristiques influençant la circulation des macromolécules dans l’organisme. La taille des molécules, leur point de trouble ainsi que la présence d’un segment hydrophobe à l’extrémité des chaînes se sont avérés déterminants. Le seuil de filtration glomérulaire du polymère a été évalué à 32 000 g/mol. Finalement, l’analyse PK a permis de s’assurer que les complexes formés par la fixation du polymère à la surface des liposomes restaient stables dans le sang, après injection par voie intraveineuse. Ces données ont établi qu’il était possible de synthétiser un polymère pouvant être adéquatement éliminé par filtration rénale et que les liposomes sensibles au pH préparés avec celui-ci demeuraient intacts dans l’organisme. En second lieu, l’analyse PK a été utilisée dans le développement de liposomes possédant un gradient de pH transmembranaire pour le traitement des intoxications médicamenteuses. Une formulation a été développée et optimisée in vitro pour capturer un médicament modèle, le diltiazem (DTZ). La formulation liposomale s’est avérée 40 fois plus performante que les émulsions lipidiques utilisées en clinique. L’analyse PK des liposomes a permis de confirmer la stabilité de la formulation in vivo et d’analyser l’influence des liposomes sur la circulation plasmatique du DTZ et de son principal métabolite, le desacétyldiltiazem (DAD). Il a été démontré que les liposomes étaient capables de capturer et de séquestrer le principe actif dans la circulation sanguine lorsque celui-ci était administré, par la voie intraveineuse. L’injection des liposomes 2 minutes avant l’administration du DTZ augmentait significativement l’aire sous la courbe du DTZ et du DAD tout en diminuant leur clairance plasmatique et leur volume de distribution. L’effet de ces modifications PK sur l’activité pharmacologique du médicament a ensuite été évalué. Les liposomes ont diminué l’effet hypotenseur du principe actif administré en bolus ou en perfusion sur une période d’une heure. Au cours de ces travaux, l’analyse PK a servi à établir la preuve de concept que des liposomes possédant un gradient de pH transmembranaire pouvaient modifier la PK d’un médicament cardiovasculaire et en diminuer l’activité pharmacologique. Ces résultats serviront de base pour le développement de la formulation destinée au traitement des intoxications médicamenteuses. Ce travail souligne la pertinence d’utiliser l’analyse PK dans la mise au point de vecteurs pharmaceutiques destinés à des applications variées. À ce stade de développement, l’aspect prédictif de l’analyse n’a pas été exploité, mais le côté descriptif a permis de comparer adéquatement diverses formulations et de tirer des conclusions pertinentes quant à leur devenir dans l’organisme.

Copper Doped Methylene Blue Sensitized Poly(vinyl alcohol)–Acrylamide Films for Stable Diffraction Efficiency

Copper doped methylene blue sensitized poly(vinyl alcohol) (MBPVA)–acrylamide films were fabricated to improve the storage life of recorded gratings. The films were fabricated using gravity settling method and the copper chloride concentration was optimized as 3:18 10 3 mol/l for a dye concentration of 6:2 10 4 mol/l. The gratings recorded on the optimized film constitution could be stored for months with stable diffraction efficiency (24%) without any chemical or thermal fixing techniques. The resolution of the material is found to be unaffected with the addition of copper chloride.

Copper Doped Methylene Blue Sensitized Poly(vinyl alcohol)–Acrylamide Films for Stable Diffraction Efficiency

Copper doped methylene blue sensitized poly(vinyl alcohol) (MBPVA)–acrylamide films were fabricated to improve the storage life of recorded gratings. The films were fabricated using gravity settling method and the copper chloride concentration was optimized as 3:18 10 3 mol/l for a dye concentration of 6:2 10 4 mol/l. The gratings recorded on the optimized film constitution could be stored for months with stable diffraction efficiency (24%) without any chemical or thermal fixing techniques. The resolution of the material is found to be unaffected with the addition of copper chloride.

Copper Doped Methylene Blue Sensitized Poly(vinyl alcohol)–Acrylamide Filmsfor Stable Diffraction Efficiency

Copper doped methylene blue sensitized poly(vinyl alcohol) (MBPVA)–acrylamide films were fabricated to improve the storage life of recorded gratings. The films were fabricated using gravity settling method and the copper chloride concentration was optimized as 3:18 10 3 mol/l for a dye concentration of 6:2 10 4 mol/l. The gratings recorded on the optimized film constitution could be stored for months with stable diffraction efficiency (24%) without any chemical or thermal fixing techniques. The resolution of the material is found to be unaffected with the addition of copper chloride.

Studies on Advanced Oxidation Processes for the Removal of Acetamiprid from Wastewater

Pollution of water with pesticides has become a threat to the man, material and environment. The pesticides released to the environment reach the water bodies through run off. Industrial wastewater from pesticide manufacturing industries contains pesticides at higher concentration and hence a major source of water pollution. Pesticides create a lot of health and environmental hazards which include diseases like cancer, liver and kidney disorders, reproductive disorders, fatal death, birth defects etc. Conventional wastewater treatment plants based on biological treatment are not efficient to remove these compounds to the desired level. Most of the pesticides are phyto-toxic i.e., they kill the microorganism responsible for the degradation and are recalcitrant in nature. Advanced oxidation process (AOP) is a class of oxidation techniques where hydroxyl radicals are employed for oxidation of pollutants. AOPs have the ability to totally mineralise the organic pollutants to CO2 and water. Different methods are employed for the generation of hydroxyl radicals in AOP systems. Acetamiprid is a neonicotinoid insecticide widely used to control sucking type insects on crops such as leafy vegetables, citrus fruits, pome fruits, grapes, cotton, ornamental flowers. It is now recommended as a substitute for organophosphorous pesticides. Since its use is increasing, its presence is increasingly found in the environment. It has high water solubility and is not easily biodegradable. It has the potential to pollute surface and ground waters. Here, the use of AOPs for the removal of acetamiprid from wastewater has been investigated. Five methods were selected for the study based on literature survey and preliminary experiments conducted. Fenton process, UV treatment, UV/ H2O2 process, photo-Fenton and photocatalysis using TiO2 were selected for study. Undoped TiO2 and TiO2 doped with Cu and Fe were prepared by sol-gel method. Characterisation of the prepared catalysts was done by X-ray diffraction, scanning electron microscope, differential thermal analysis and thermogravimetric analysis. Influence of major operating parameters on the removal of acetamiprid has been investigated. All the experiments were designed using central compoiste design (CCD) of response surface methodology (RSM). Model equations were developed for Fenton, UV/ H2O2, photo-Fenton and photocatalysis for predicting acetamiprid removal and total organic carbon (TOC) removal for different operating conditions. Quality of the models were analysed by statistical methods. Experimental validations were also done to confirm the quality of the models. Optimum conditions obtained by experiment were verified with that obtained using response optimiser. Fenton Process is the simplest and oldest AOP where hydrogen peroxide and iron are employed for the generation of hydroxyl radicals. Influence of H2O2 and Fe2+ on the acetamiprid removal and TOC removal by Fenton process were investigated and it was found that removal increases with increase in H2O2 and Fe2+ concentration. At an initial concentration of 50 mg/L acetamiprid, 200 mg/L H2O2 and 20 mg/L Fe2+ at pH 3 was found to be optimum for acetamiprid removal. For UV treatment effect of pH was studied and it was found that pH has not much effect on the removal rate. Addition of H2O2 to UV process increased the removal rate because of the hydroxyl radical formation due to photolyis of H2O2. An H2O2 concentration of 110 mg/L at pH 6 was found to be optimum for acetamiprid removal. With photo-Fenton drastic reduction in the treatment time was observed with 10 times reduction in the amount of reagents required. H2O2 concentration of 20 mg/L and Fe2+ concentration of 2 mg/L was found to be optimum at pH 3. With TiO2 photocatalysis improvement in the removal rate was noticed compared to UV treatment. Effect of Cu and Fe doping on the photocatalytic activity under UV light was studied and it was observed that Cu doping enhanced the removal rate slightly while Fe doping has decreased the removal rate. Maximum acetamiprid removal was observed for an optimum catalyst loading of 1000 mg/L and Cu concentration of 1 wt%. It was noticed that mineralisation efficiency of the processes is low compared to acetamiprid removal efficiency. This may be due to the presence of stable intermediate compounds formed during degradation Kinetic studies were conducted for all the treatment processes and it was found that all processes follow pseudo-first order kinetics. Kinetic constants were found out from the experimental data for all the processes and half lives were calculated. The rate of reaction was in the order, photo- Fenton>UV/ H2O2>Fenton> TiO2 photocatalysis>UV. Operating cost was calculated for the processes and it was found that photo-Fenton removes the acetamiprid at lowest operating cost in lesser time. A kinetic model was developed for photo-Fenton process using the elementary reaction data and mass balance equations for the species involved in the process. Variation of acetamiprid concentration with time for different H2O2 and Fe2+ concentration at pH 3 can be found out using this model. The model was validated by comparing the simulated concentration profiles with that obtained from experiments. This study established the viability of the selected AOPs for the removal of acetamiprid from wastewater. Of the studied AOPs photo- Fenton gives the highest removal efficiency with lowest operating cost within shortest time.

Transport and distribution of lindane and simazine in a riverine environment: measurements in bed sediments and modelling

Aquatic sediments often remove hydrophobic contaminants from fresh waters. The subsequent distribution and concentration of contaminants in bed sediments determines their effect on benthic organisms and the risk of re-entry into the water and/or leaching to groundwater. This study examines the transport of simazine and lindane in aquatic bed sediments with the aim of understanding the processes that determine their depth distribution. Experiments in flume channels (water flow of 10 cm s(-1)) determined the persistence of the compounds in the absence of sediment with (a) de-ionised water and (b) a solution that had been in contact with river sediment. In further experiments with river bed sediments in light and dark conditions, measurements were made of the concentration of the compounds in the overlying water and the development of bacterial/algal biofilms and bioturbation activity. At the end of the experiments, concentrations in sediments and associated pore waters were determined in sections of the sediment at 1 mm resolution down to 5 mm and then at 10 mm resolution to 50 mm depth and these distributions analysed using a sorption-diffusion-degradation model. The fine resolution in the depth profile permitted the detection of a maximum in the concentration of the compounds in the pore water near the surface, whereas concentrations in the sediment increased to a maximum at the surface itself. Experimental distribution coefficients determined from the pore water and sediment concentrations indicated a gradient with depth that was partly explained by an increase in organic matter content and specific surface area of the solids near the interface. The modelling showed that degradation of lindane within the sediment was necessary to explain the concentration profiles, with the optimum agreement between the measured and theoretical profiles obtained with differential degradation in the oxic and anoxic zones. The compounds penetrated to a depth of 40-50 rum over a period of 42 days. (C) 2004 Society of Chemical Industry.

Long-lived halocarbon trends and budgets from atmospheric chemistry modelling constrained with measurements in polar firn

The budgets of seven halogenated gases (CFC-11, CFC-12, CFC-113, CFC-114, CFC-115, CCl4 and SF6) are studied by comparing measurements in polar firn air from two Arctic and three Antarctic sites, and simulation results of two numerical models: a 2-D atmospheric chemistry model and a 1-D firn diffusion model. The first one is used to calculate atmospheric concentrations from emission trends based on industrial inventories; the calculated concentration trends are used by the second one to produce depth concentration profiles in the firn. The 2-D atmospheric model is validated in the boundary layer by comparison with atmospheric station measurements, and vertically for CFC-12 by comparison with balloon and FTIR measurements. Firn air measurements provide constraints on historical atmospheric concentrations over the last century. Age distributions in the firn are discussed using a Green function approach. Finally, our results are used as input to a radiative model in order to evaluate the radiative forcing of our target gases. Multi-species and multi-site firn air studies allow to better constrain atmospheric trends. The low concentrations of all studied gases at the bottom of the firn, and their consistency with our model results confirm that their natural sources are small. Our results indicate that the emissions, sinks and trends of CFC-11, CFC-12, CFC-113, CFC-115 and SF6 are well constrained, whereas it is not the case for CFC-114 and CCl4. Significant emission-dependent changes in the lifetimes of halocarbons destroyed in the stratosphere were obtained. Those result from the time needed for their transport from the surface where they are emitted to the stratosphere where they are destroyed. Efforts should be made to update and reduce the large uncertainties on CFC lifetimes.

Kinetic multi-layer model of aerosol surface and bulk chemistry (KM-SUB): the influence of interfacial transport and bulk diffusion on the oxidation of oleic acid by ozone

We present a novel kinetic multi-layer model that explicitly resolves mass transport and chemical reaction at the surface and in the bulk of aerosol particles (KM-SUB). The model is based on the PRA framework of gas-particle interactions (Poschl-Rudich-Ammann, 2007), and it includes reversible adsorption, surface reactions and surface-bulk exchange as well as bulk diffusion and reaction. Unlike earlier models, KM-SUB does not require simplifying assumptions about steady-state conditions and radial mixing. The temporal evolution and concentration profiles of volatile and non-volatile species at the gas-particle interface and in the particle bulk can be modeled along with surface concentrations and gas uptake coefficients. In this study we explore and exemplify the effects of bulk diffusion on the rate of reactive gas uptake for a simple reference system, the ozonolysis of oleic acid particles, in comparison to experimental data and earlier model studies. We demonstrate how KM-SUB can be used to interpret and analyze experimental data from laboratory studies, and how the results can be extrapolated to atmospheric conditions. In particular, we show how interfacial and bulk transport, i.e., surface accommodation, bulk accommodation and bulk diffusion, influence the kinetics of the chemical reaction. Sensitivity studies suggest that in fine air particulate matter oleic acid and compounds with similar reactivity against ozone (carbon-carbon double bonds) can reach chemical lifetimes of many hours only if they are embedded in a (semi-)solid matrix with very low diffusion coefficients (< 10(-10) cm(2) s(-1)). Depending on the complexity of the investigated system, unlimited numbers of volatile and non-volatile species and chemical reactions can be flexibly added and treated with KM-SUB. We propose and intend to pursue the application of KM-SUB as a basis for the development of a detailed master mechanism of aerosol chemistry as well as for the derivation of simplified but realistic parameterizations for large-scale atmospheric and climate models.

Kinetic multi-layer model of aerosol surface and bulk chemistry (KM-SUB): the influence of interfacial transport and bulk diffusion on the oxidation of oleic acid by ozone

We present a novel kinetic multi-layer model that explicitly resolves mass transport and chemical reaction at the surface and in the bulk of aerosol particles (KM-SUB). The model is based on the PRA framework of gas–particle interactions (P¨oschl et al., 5 2007), and it includes reversible adsorption, surface reactions and surface-bulk exchange as well as bulk diffusion and reaction. Unlike earlier models, KM-SUB does not require simplifying assumptions about steady-state conditions and radial mixing. The temporal evolution and concentration profiles of volatile and non-volatile species at the gas-particle interface and in the particle bulk can be modeled along with surface 10 concentrations and gas uptake coefficients. In this study we explore and exemplify the effects of bulk diffusion on the rate of reactive gas uptake for a simple reference system, the ozonolysis of oleic acid particles, in comparison to experimental data and earlier model studies. We demonstrate how KM-SUB can be used to interpret and analyze experimental data from laboratory stud15 ies, and how the results can be extrapolated to atmospheric conditions. In particular, we show how interfacial transport and bulk transport, i.e., surface accommodation, bulk accommodation and bulk diffusion, influence the kinetics of the chemical reaction. Sensitivity studies suggest that in fine air particulate matter oleic acid and compounds with similar reactivity against ozone (C=C double bonds) can reach chemical lifetimes of 20 multiple hours only if they are embedded in a (semi-)solid matrix with very low diffusion coefficients (10−10 cm2 s−1). Depending on the complexity of the investigated system, unlimited numbers of volatile and non-volatile species and chemical reactions can be flexibly added and treated with KM-SUB. We propose and intend to pursue the application of KM-SUB 25 as a basis for the development of a detailed master mechanism of aerosol chemistry as well as for the derivation of simplified but realistic parameterizations for large-scale atmospheric and climate models.

A preliminary investigation of the impact of catechol-O-methyltransferase genotype on the absorption and metabolism of green tea catechins

Purpose Green tea is thought to possess many beneficial effects on human health. However, the extent of green tea polyphenol biotransformation may affect its proposed therapeutic effects. Catechol-O-methyltransferase (COMT), the enzyme responsible for polyphenolic methylation, has a common polymorphism in the genetic code at position 158 reported to result in a 40% reduction in enzyme activity in in vitro studies. The current preliminary study was designed to investigate the impact of COMT genotype on green tea catechin absorption and metabolism in humans. Methods Twenty participants (10 of each homozygous COMT genotype) were recruited, and plasma concentration profiles were produced for epigallocatechin gallate (EGCG), epigallocatechin (EGC), epicatechin gallate (ECG), epicatechin (EC) and 4′-O-methyl EGCG after 1.1 g of Sunphenon decaffeinated green tea extract (836 mg green tea catechins), with a meal given after 60 min. Results For the entire group, EGCG, EGC, EC, ECG and 4′-O-methyl EGCG reached maximum concentrations of 1.09, 0.41, 0.33, 0.16 and 0.08 μM at 81.5, 98.5, 99.0, 85.5 and 96.5 min, respectively. Bimodal curves were observed for the non-gallated green tea catechins EGC and EC as opposed to single-peaked curves for the gallated green tea catechins EGCG and ECG. No significant parametric differences between COMT genotype groups were found. Conclusions In conclusion, the COMT Val(158/108)Met does not appear to have a dramatic influence on EGCG absorption and elimination. However, further pharmacokinetic research is needed to substantiate these findings.