Comparison of MB fraction of creatine kinase mass and troponin I serum levels with necropsy findings in acute myocardial infarction

Serum levels of troponin and heart-related fraction of creatine kinase (CK-MB) mass are used as diagnostic and prognostic criteria in myocardial infarction, but the relation between those levels and-the necropsy-determined size of necrosis has not been tested in human beings. In this retrospective study, 1-cm-thick transverse sections of the ventricles were cut from the base to the apex in the necropsy hearts of 27 patients aged 47 to 86 years (mean 66, median 69; 19 men). Total and necrotic areas were measured using a computer-linked image analysis system. The weights of the necrotic areas were also calculated. The correlations of the areas and weights of necrotic myocardium with the highest serum values of CK-MB mass and troponin 1, which had been quantified during life by chemiluminescence immunoassays, were verified by Pearson`s test; results were considered significant at p <= 50.05. Significant correlations were detected between CK-MB mass peak and infarct size (r = 0.63, p < 0.01) and weight (r = 0.69, p < 0.01) and between CK-MB mass and highest troponin level (r = 0.73, p < 0.01); however, the correlations between highest troponin level and myocardial infarct size (r = 0.31, p = 0.11) and weight (r = 0.35, p = 0.07) were small and nonsignificant. In conclusion, despite the well-established role of serum levels of troponin as a diagnostic tool for myocardial infarction, their highest values showed poor correlations with the extent of infarct. In contrast, the highest serum level of CK-MB mass was well correlated with myocardial infarct size. (c) 2008 Elsevier Inc. All rights reserved.

The IWA Anaerobic Digestion Model No 1 (ADM1)

The IWA Anaerobic Digestion Modelling Task Group was established in 1997 at the 8th World Congress on,Anaerobic Digestion (Sendai, Japan) with the goal of developing a generalised anaerobic digestion model. The structured model includes multiple steps describing biochemical as well as physicochemical processes. The biochemical steps include disintegration from homogeneous particulates to carbohydrates, proteins and lipids; extracellular hydrolysis of these particulate substrates to sugars, amino acids, and long chain fatty acids (LCFA), respectively; acidogenesis from sugars and amino acids to volatile fatty acids (VFAs) and hydrogen; acetogenesis of LCFA and VFAs to acetate; and separate methanogenesis steps from acetate and hydrogen/CO2. The physico-chemical equations describe ion association and dissociation, and gas-liquid transfer. Implemented as a differential and algebraic equation (DAE) set, there are 26 dynamic state concentration variables, and 8 implicit algebraic variables per reactor vessel or element. Implemented as differential equations (DE) only, there are 32 dynamic concentration state variables.

Analysis of the microbial community structure and function of a laboratory scale enhanced biological phosphorus removal reactor

A laboratory scale sequencing batch reactor (SBR) operating for enhanced biological phosphorus removal (EBPR) and fed with a mixture of volatile fatty acids (VFAs) showed stable and efficient EBPR capacity over a four-year-period. Phosphorus (P), poly-beta-hydroxyalkanoate (PHA) and glycogen cycling consistent with classical anaerobic/aerobic EBPR were demonstrated with the order of anaerobic VFA uptake being propionate, acetate then butyrate. The SBR was operated without pH control and 63.67+/-13.86 mg P l(-1) was released anaerobically. The P% of the sludge fluctuated between 6% and 10% over the operating period (average of 8.04+/-1.31%). Four main morphological types of floc-forming bacteria were observed in the sludge during one year of in-tensive microscopic observation. Two of them were mainly responsible for anaerobic/aerobic P and PHA transformations. Fluorescence in situ hybridization (FISH) and post-FISH chemical staining for intracellular polyphosphate and PHA were used to determine that 'Candidatus Accumulibacter phosphatis' was the most abundant polyphosphate accumulating organism (PAO), forming large clusters of coccobacilli (1.0-1.5 mum) and comprising 53% of the sludge bacteria. Also by these methods, large coccobacillus-shaped gammaproteobacteria (2.5-3.5 mum) from a recently described novel cluster were glycogen-accumulating organisms (GAOs) comprising 13% of the bacteria. Tetrad-forming organisms (TFOs) consistent with the 'G bacterium' morphotype were alphaproteobacteria , but not Amaricoccus spp., and comprised 25% of all bacteria. According to chemical staining, TFOs were occasionally able to store PHA anaerobically and utilize it aerobically.

Nitrifying microbial community analysis of nitrite accumulating biofilm reactor by fluorescence in situ hybridization

Biological nitrogen removal via nitrite pathway in wastewater treatment is very important especially in the cost of aeration and as an electron donor for denitrification. Wastewater nitrification and nitrite accumulations were carried out in a biofilm reactor. The biofilm reactor showed almost complete nitrification and most of the oxidized ammonium was present as nitrite at the ammonium load of 1.2 kg N/m3/d. Nitrite accumulation was achieved by the selective inhibition of nitrite oxidizers by free ammonia and oxygen limitation. Nitrite oxidation activity was recovered as soon as the inhibition factor was removed. Fluorescence in situ hybridization studies of the nitrite accumulating biofilm system have shown that genus Nitrosomonas which is specifically hybridized with probe NSM 156 was the dominant nitrifying bacteria while Nitrospira was less abundant than those of normal nitrification systems. Further FISH analysis showed that the combinations of Nitrosomonas and Nitrospira cells were identified as important populations of nitrifying bacteria in an autotrophic nitrifying biofilm system.

Biofiltration of Air/Styrene and Air/Styrene/Acetone mixtures in a bubble column reactor

The goal of this work was the treatment of polluted waste gases in a bubble column reactor (BCR), in order to determinate the maximum value of reactor’s efficiency (RE), varying the inlet concentration (C in) of the pollutants. The gaseous mixtures studied were: (i) air with styrene and (ii) air with styrene and acetone. The liquid phase used to contain the biomass in the reactor was a basal salt medium (BSM), fundamental for the microorganisms’ development. The reactor used in this project consists of a glass column of 620mm height and inside diameter 75mm. In all essays there were continually measured: pH, dissolved oxygen and liquid’s temperature. Temperature and pH were controlled (T=24ºC, 7.0 ≤ pH ≤ 7.7). In all experiments the liquid volume (including the biomass) used in the reactor was kept constant (1.5L) as well as the total gas flowrate (1 L/min). Concerning the goal of the work, some parameters were calculated: the organic load (OL), removal efficiency (RE), elimination capacity (EC), biomass concentration (xf) and dry biomass concentration (Xdw). In a first series of experiments, the gas mixture used was air with styrene, varying its concentration from 191 mg.m-3 to 6500 mg.m-3.It was concluded that the RE maximum value (97%) was obtained for C in Sty = 4200 mg.m-3. For the maximum tested value of C in Sty, RE obtained was 20%. In a second step, the gaseous mixture included acetone, varying C in Sty between 225 mg.m-3 and 2659 mg.m-3 and C in Ac between 153mg.m-3 and 1389 mg.m-3. The aim of these tests was the determination of C in Ac for which RE was maximum, obtaining C in Ac = 750 mg.m-3. A third series of experiments was performed, in which C in Ac was maintained equal to that value and C in Sty was varied until higher values (5422 mg.m-3). RE maximum values obtained in this last series were 100% for styrene and 40% for acetone. One important conclusion is the fact that the microorganisms available degrade better styrene than acetone. On the ambit of this study, it was possible to identify the species available in biomass: Xanthobacter antotrophicus py2, Enterobacter aerogenes, Nocardia, Corynebacterium Spp., Rhodococcus rhodochrous e Pseudomonas Sp.

Contribuição para o estudo da modelação da digestão anaeróbia de resíduos sólidos, estudo da influência da geometria do reactor na cinética do processo

O presente trabalho tem como objectivo contribuir para o estudo do desenvolvimento de um modelo matemático aplicado à digestão anaeróbia de resíduos sólidos, que incorpore os condicionamentos da geometria dos reactores e a sua influência na cinética do processo biológico. Nesse sentido, o trabalho propõe-se avaliar o comportamento cinético de três reactores, com o mesmo volume mas com diferentes relações tridimensionais, utilizando o mesmo substrato, e idênticos parâmetros ambientais e operacionais de funcionamento. Pretendeu-se estudar em que medida a relação do comprimento, largura e altura de um reactor pode interferir nas taxas de remoção de substrato, condicionando a respectiva difusão na biomassa e crescimento dos microrganismos. Considera-se que este aspecto é do maior interesse para o desenvolvimento de um modelo cinético, podendo minimizar desvios inerentes à própria modelação de processos biológicos complexos. A geometria do reactor, que se correlaciona com uma determinada relação tridimensional, pode constituir um parâmetro importante, que se designou por Kcig (Constante de Inibição Geométrica), dada a influência que poderá exercer na cinética do processo biológico. A sua avaliação, parametrização e consequente modelação, deverá facilitar a escolha da relação comprimento/largura/altura mais adequada, de forma a optimizar o funcionamento operacional do reactor. O plano experimental desenvolveu-se em duas fases, utilizando-se dois substratos com graus distintos de dificuldade de utilização pelos microrganismos, nomeadamente: Fase 1 (glucose), Fase 2 (FORSU e relva). Concluiu-se que a cinética do processo é influenciada pela relação entre as áreas de separação de biogás/biomassa (As) e de contacto biomassa/reactor (Ac), que interferem na geometria do reactor. Assim, através dos resultados das fases 1 e 2 pode observar-se que a variação da taxa de remoção de substrato se aproxima de uma função de saturação, pelo que se propõe uma adaptação do modelo de Monod, através de um formalismo que incorpora uma grandeza adimensional, Kcig, para reflectir o efeito da geometria do reactor. Verificou-se que a equação adoptada para Kcig se mostrou adequada, o que permitiu, através do modelo de Monod ajustado, estimar os valores de rx máx e Ks que se admite estarem mais próximos dos verdadeiros, embora se considere que apenas se pretende corrigi-los em função do efeito da geometria do reactor. Por outro lado, o estudo permitiu identificar um valor de Kcig para o reactor de 2,5 L, a partir do qual poderá não ser interessante a relação entre a taxa de remoção de substrato e a área de construção do reactor.

Importância da interação entre a integrina Mac-1 dos leucócitos e a glicoproteína Iba das plaquetas para o recrutamento de leucócitos pelas plaquetas e para a resposta inflamatória à lesão vascular

OBJETIVO: Avaliar a importância da interação entre a integrina Mac-1 dos leucócitos (a Mb 2) e a glicoproteína (GP) Iba das plaquetas para o recrutamento de leucócitos após a lesão vascular e o efeito da neutralização da interação Mac-1-GPIba sobre a proliferação celular e a hiperplasia neointimal desencadeadas por lesão vascular. MÉTODOS: Um peptídeo denominado M2 ou anticorpo anti-M2 foi desenvolvido para bloquear a interação Mac-1-GPIba . Esse peptídeo foi injetado e comparado com anticorpo-controle em camundongos C57B1/6J submetidos a lesão vascular da artéria femoral com corda-guia. Um, cinco ou 28 dias após a lesão vascular, as artérias femorais foram retiradas para a realização de morfometria e imuno-histoquímica. RESULTADOS: O bloqueio da interação Mac-1-GPIba promoveu uma redução estatisticamente significativa do número de leucócitos na camada média no primeiro dia após a lesão vascular (controle: 7,9±5,0% do total de células versus anti-M2: 2,0±1,6%, p=0,021), bem como determinou uma diminuição estatisticamente significativa do acúmulo de leucócitos na neoíntima em cinco e 28 dias (controle: 42,3±12,9% versus anti-M2: 24,6±10,8%, p=0,047 e controle: 7,9±3,0% versus anti-M2: 3,3±1,3%, p=0,012; respectivamente). A proliferação celular na camada média do vaso em cinco dias pós-lesão foi reduzida com o bloqueio da interação Mac-1-GPIba (controle: 5,0±2,9% do total de células versus anti-M2: 1,8±0,5%; p=0,043), assim como houve diminuição significativa da proliferação celular na camada íntima do vaso em 28 dias (controle: 3,8±1,7% versus anti-M2: 2,0±1,2%; p=0,047). O bloqueio da interação Mac-1-GPIba também determinou uma redução estatisticamente significativa do espessamento intimal em 28 dias pós-lesão (controle: 10.395±3.549 µm² versus anti-M2: 4.561±4.915 µm²; p=0,012). CONCLUSÃO: O recrutamento de leucócitos após a lesão vascular é dependente da interação Mac-1-GPIba e a neutralização dessa interação inibe a proliferação celular e a formação neointimal.

Comparação entre troponina I cardíaca e CK-MB massa em síndrome coronariana aguda sem supra de ST

FUNDAMENTO: Há incertezas do valor prognóstico comparativo entre troponina I cardíaca (cTnI) e CK-MB em síndrome coronariana aguda (SCA). OBJETIVO: Comparar o valor prognóstico entre a cTnI e a CK-MB massa em pacientes com SCA sem supradesnível do segmento ST. MÉTODOS: Foram analisados 1.027 pacientes, de modo prospectivo, em um centro terciário de cardiologia. Combinações dos biomarcadores foram examinadas: cTnI normal, CK-MB massa normal (65,5%); cTnI normal, CK-MB massa elevada (3,9%); cTnI elevada, CK-MB massa normal (8,8%); cTnI elevada, CK-MB massa elevada (20,7%). Análise multivariada de variáveis clínicas, eletrocardiográficas e laboratoriais determinou o valor prognóstico independente dos biomarcadores para o evento de morte ou (re)infarto em 30 dias. RESULTADOS: Pacientes com pelo menos um biomarcador elevado foram mais idosos (p = 0,02) e do sexo masculino (p < 0,001). Uso prévio de aspirina (p = 0,001), betabloqueador (p = 0,003) ou estatina (p = 0,013) foi mais frequente naqueles sem elevação da cTnI. Pacientes com elevação de ambos os biomarcadores tinham mais depressão do segmento ST (p < 0,001) ou creatinina elevada (p < 0,001). Em análise multivariada com a inclusão da cTnI, a CK-MB massa não foi variável independente para o evento de morte ou (re)infarto em 30 dias (odds ratio [OR] 1,16; p = 0,71). Quando não se incluiu a cTnI, teve-se: idade (OR 1,07; p < 0,001); sexo masculino (OR 1,09; p = 0,77); diabete melito (OR 1,95; p = 0,02); acidente vascular cerebral prévio (OR 3,21; p = 0,008); creatinina elevada (OR 1,63; p = 0,002); elevação da CK-MB massa (OR 1,96; p = 0,03); estatística-C 0,77 (p < 0,001). CONCLUSÃO: Com dosagem da cTnI, a CK-MB massa pode ser dispensável para avaliação prognóstica. Na indisponibilidade da cTnI, a CK-MB massa é aceitável para decisão terapêutica.

Experimental study on n-butane partial oxidation to maleic anhydride in a solid electrolyte membrane reactor

n-Butane, Partial oxidation, Maleic anhydride, electrochemical oxygen pumping, solid electrolyte membrane reactor

Analysis of heterogeneously catalyzed ester hydrolysis reactions in a fixed-bed chromatographic reactor

Reactive Chromatography, Fixed-Bed Reactor, Heterogeneous, Hydrolysis, Ester, Catalyst, Adsorption, Ion-Exchange Resin

Spatio-temporal dynamics of glycolysis in an open spatial reactor

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2008

Precipitation of barium sulfate in a semi-batch stirred tank reactor : influence of feeding policy on particle size and morphology

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2012

Prozesse in Hochschulen mit integrierten IT-Kollaborationsumgebungen verbessern! : 1. Tagungsband 19. Juni 2009

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Electrochemical high temperature membrane reactor for the processing of hydrogen-carbon monoxide gas mixtures

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2013

Experimental and theoretical analysis of the cyclic water gas shift reactor

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2015