Electron donor sites on Y2O3 catalyst as a function of the activation temperature

Cochin University of Science and Technology

Avaliação do desempenho de adsorventes obtidos a partir de resíduos da indústria de curtumes na adsorção de poluentes

Na procura por uma solução de valorização dos resíduos gerados pela indústria de curtumes, o presente trabalho tem como principais objectivos a preparação de adsorventes a partir de resíduos desta actividade e a avaliação do seu desempenho na adsorção de poluentes. Para atingir este objectivo, inicialmente procedeu-se à carbonização das aparas de couro wet-white à temperatura de 800 ºC. Seguidamente, os carbonizados foram activados por activação química, tendo sido o hidróxido de potássio o agente activante escolhido. As razões mássicas hidróxido de potássio:precursor usadas na impregnação, foram iguais a 0,5:1 e 1:1. Para a razão 0,5:1, as temperaturas de activação escolhidas foram 700 e 800 ºC. Para a razão de impregnação 1:1, as temperaturas de activação usadas foram 700, 800 e 900 ºC. Para uma avaliação preliminar da capacidade de adsorção dos carvões activados produzidos, efectuou-se a determinação do número de azul de metileno. Este teste provou serem as amostras activadas a 900 ºC as que apresentaram melhores resultados (número de azul de metileno: 24g/100g) e as amostras activadas a 700 ºC, as que apresentaram menor capacidade de adsorção (1g/100g, para a razão de 0,5:1 e 7g/100g, para a razão de 1:1). Verificou-se também que amostras preparadas com iguais condições de activação (temperatura de activação e razão de impregnação), mas produzidas a partir de carbonizado de diferentes granulometrias, apresentaram diferentes desempenhos na adsorção de azul de metileno. As propriedades texturais dos carvões activados produzidos foram obtidas pela determinação das isotérmicas de adsorção de azoto a 77 K. Para tal, selecionaram-se quatro amostras: dois carvões activados a 800 ºC, com uma razão de impregnação de 1:1 e dois carvões activados a 900 ºC, com a mesma razão de impregnação, obtidos a partir de carbonizados com diferentes granulometrias. As isotérmicas obtidas são características de materiais essencialmente microporosos, com mesoporos e macroporos. Verificou-se também que a granulometria do precursor carbonizado influencia as propriedades texturais dos carvões activados produzidos. Para as temperaturas de activação usadas, 800 e 900 ºC, os carvões activados preparados a partir de carbonizado de menor granulometria apresentam melhores propriedades texturais. O carvão activado que apresentou maior área superficial específica foi obtido a 900 ºC, a partir de carbonizado finamente moído (SBET = 1475 m2/g). Determinadas as propriedades texturais dos carvões activados produzidos, realizaram-se ensaios de adsorção do corante CORIACIDE DARK BROWN VR, usado na indústria de curtumes com um carvão activado produzido no âmbito deste trabalho e com um carvão activado comercial NORIT ROW 0,8. A amostra de carvão activado produzida a partir de resíduos de wet-white escolhida para estes ensaios foi o carvão activado a 800 ºC, à razão de 1:1, a partir de carbonizado finamente moído (ww_800_1:1_carb.moído). Verificou-se que as quantidades adsorvidas pela amostra ww_800_1:1_carb.moído variaram entre os valores 7,47 e 32,07 mgcorante/gcarvão activado. Quanto ao carvão activado comercial, as quantidades adsorvidas situaram-se entre 8,95 e 69,13 mgcorante/gcarvão activado. Assim, conclui-se que o carvão activado comercial apresentou melhor desempenho na adsorção do corante da indústria de curtumes. Os carvões activados obtidos revelaram-se materiais essencialmente microporosos, com capacidade de adsorção de poluentes, como por exemplo corantes, no entanto o seu desempenho seria mais eficaz na adsorção de pequenas moléculas devido ao elevado volume de microporos que apresentaram.

Preparação de materiais de carbono para a adsorção de compostos orgânicos voláteis (COV).

A presente dissertação estudou a produção de carvão ativado a partir de resíduo de wet-blue, proveniente da indústria de curtumes, para a adsorção de compostos orgânicos voláteis, nomeadamente o acetato de etilo. Este estudo teve como principais objetivos: a otimização das condições de preparação de carvões ativados a partir deste tipo de resíduo; a avaliação do seu desempenho na adsorção do acetato de etilo e a correlação das propriedades texturais dos adsorventes com o seu desempenho na adsorção do COV. O método de ativação para a preparação dos carvões ativados foi a ativação química com hidróxido de potássio. Nesta etapa foi estudado o efeito da temperatura de ativação e da razão de impregnação KOH:precursor nas propriedades texturais. Nestes ensaios observou-se uma diminuição do rendimento de carbonizado com o aumento da temperatura de ativação e da razão KOH:precursor. Para a caracterização dos carvões ativados foram determinados os seus parâmetros texturais a partir das isotérmicas de adsorção/dessorção de N2 a 77 K. O carvão ativado com melhores propriedades texturais foi o ativado a 900ºC e com razão de impregnação de 3:1, m ca_900 3:1, com área superficial específica de 1902 m2/g, seguindo-se o carvão preparado a 800 ºC e com a mesma razão de impregnação, m ca_800 3:1, com área superficial específica de 1830 m2/g. Por fim, foi avaliado o desempenho do carvão ativado selecionado, m ca_800 3:1, na remoção de acetato de etilo de uma corrente gasosa. Foram efetuados ensaios de adsorção/ dessorção de acetato de etilo e o modelo de Langmuir foi ajustado aos resultados experimentais obtidos, tendo-se determinado uma capacidade de saturação de 500 mgCOV/ gadsorvente.

Preparação de carvão ativado em baixas temperaturas de carbonização a partir de rejeitos de café: utilização de FeCl3 como agente ativante

Ferric chloride as a new activating agent was used to obtain activated carbons from agroindustrial waste. This material was prepared at three temperatures of pyrolysis, 200, 280 and 400 ºC. The carbonaceous materials obtained after the activation processes showed high specific surface areas (BET), with values higher than 900 m² g-1. The materials showed different behaviors in the adsorption of methylene blue dye and reactive red textile dye in water solutions. An important fact in the use of FeCl3 as an activating agent is that the activation temperature is at 280 ºC, well below of those commonly employed in chemical or physical activations described in the literature.

The Steady-State and Transient Characteristic Analysis of Thermal Fixing a Photorefractive Hologram Grating in Lithium Niobate

The transient interaction between a refraction index grating and light beams during simultaneous writing and thermal fixing of a photorefractive hologram is investigated. With a diffusion- and photovoltaic-dominated carrier transport mechanism and carrier thermal activation (temperature dependent) considered in Fe:LiNbO3 crystal, from the standpoint of field-material coupling, the theoretical thermal fixing time and the space-charge field buildup, spatial distribution, and temperature dependence are given numerically by combining the band transport model with mobile ions with the coupled-wave equation

Surface acidity and catalytic activity of sulphated samaria

We have investigated the changes in surface acidity/basicity and catalytic pro~erties of samarium oxide due to surface modification by SO42- ion. The acidity/basicity of the catalysts is determined by titration method using Hammett indicators. Esterification of acetic acid by n-butanol is chosen as a test reaction. Sm203, owing to its high basicity and low acidity, does not catalyze the reaction. But sulphated Sm20J catalyzes the esterification reaction effectively. Activation temperature does not have much effect on the acidity of sulphated samaria.

Surface electron properties and catalytic activity of cerium-zirconium mixed oxides

The electron donating properties, surface acidity/ basicity and catalytic activity of cerium - zirconium mixed oxides at various compositions have been reported at an activation temperature of 500 degree C. The catalytic activity for the esterification of acetic acid with n-butanol has heen correlated with electron donating properties and surface acidity/basicity of the oxides.

Surface acidity/basicity of yttria and its mixed oxides with alumina catalysts

Acid/base strength distribution of Y2O3 and its mixed oxides with alumina catalysts are measured on Hammett acidity function scale and expressed in terms of H0max value. Basicity of Y2O3 increases with increase in activation temperature and for mixed oxides the basicity increases with increase in concentration of Y2O3, in the catalyst.

Avaliação da capacidade de adsorção do CO2 em zeólita 12X com gases sintéticos e originados da pirólise do lodo de esgoto

This work depicts a study of the adsorption of carbon dioxide on zeolite 13X. The activities were divided into four stages: study batch adsorption capacity of the adsorbent with synthetic CO2 (4%), fixed bed dynamic evaluation with the commercial mixture of gases (4% CO2, 1.11% CO, 1 2% H2, 0.233% CH4, 0.1% C3, 0.0233% C4 argon as inert closing balance), fixed bed dynamic modeling and evaluation of the breakthrough curve of CO2 originated from the pyrolysis of sewage sludge. The sewage sludge and the adsorbent were characterized by analysis TG / DTA, SEM, XRF and BET. Adsorption studies were carried out under the following operating conditions: temperature 40 °C (for the pyrolysis of the sludge T = 600 °C), pressures of 0.55 to 5.05 bar (batch process), flow rate of the gaseous mixture between 50 - 72 ml/min and the adsorbent masses of 10, 15 and 20 g (fixed bed process). The time for the adsorption batch was 7 h and on the fixed bed was around 180 min. The results of this study showed that in batch adsorption process step with zeolite 13X is efficient and the mass of adsorbed CO2 increases with the increases pressure, decreases with temperature increases and rises due the increase of activation temperature adsorbent. In the batch process were evaluated the breakthrough curves, which were compared with adsorption isotherms represented by the models of Langmuir, Freündlich and Toth. All models well adjusted to the experimental points, but the Langmuir model was chosen in view of its use in the dynamic model does not have implications for adsorption (indeterminacy and larger number of parameters such as occurred with others) in solving the equation. In the fixed bed dynamic study with the synthetic gas mixture, 20 g of mass adsorbent showed the maximum adsorption percentage 46.7% at 40 °C temperature and 50 mL/min of flow rate. The model was satisfactorily fitted to the three breakthrough curves and the parameters were: axial dispersion coefficient (0.0165 dm2/min), effective diffusivity inside the particle (dm2/min 0.0884) and external transfer coefficient mass (0.45 dm/min). The breakthrough curve for CO2 in the process of pyrolysis of the sludge showed a fast saturation with traces of aerosols presents in the gas phase into the fixed bed under the reaction process

Sensor for hydrogen peroxide based on Prussian Blue modified electrode: Improvement of the operational stability

Improvement of the operational stability of amperometric sensors based on Prussian Blue (PB) modified glassy carbon electrodes is presented. The long term performance of the sensors was evaluated by injection of hydrogen peroxide (5 μM in potassium buffer) solutions in a flow-injection system during a period of 5-10 h. The following parameters were investigated and correlated with the performance of the sensor: the times for electrodeposition and electrochemical activation, temperature, storage time, pH, composition of the buffer solution and of volume sample injected. These analytical characteristics of the modified electrode can be emphasized: initial sensitivity of 0.3 A cm-2 M-1, detection limit of ca. 0.5 μM, precise results (r.s.d.< 1.5%) and possibility to carry out around 50 samples (50 μL) per hour.

Temperaturas de acionamento de condicionadores de ar e ventiladores

Este trabalho apresenta os resultados iniciais de uma pesquisa, descrevendo o comportamento de usuários de edifícios de escritórios em relação às temperaturas de acionamento de ventiladores e aparelhos condicionadores de ar. Medições foram realizadas em quatro salas administrativas do Instituto de Arquitetura e Urbanismo de São Carlos – IAU/USP, nas quais foram registradas as temperaturas internas do ar e o momento de acionamento dos referidos equipamentos. Os valores registrados foram comparados à temperatura externa e à faixa de temperaturas de conforto descrita pela norma ASHRAE 55/2004. As temperaturas registradas de acionamento dos aparelhos condicionadores de ar e ventiladores são similares e estão dentro da faixa considerada confortável pela referida norma.

Entwicklung, Aufbau und Messungen eines schnellen Eiskeimzählers

Im Rahmen dieser Arbeit wurde ein neuer Eiskeimzähler FINCH (Fast Ice Nucleus CHamber) entwickelt und erste Messungen von verschiedenen Testaerosolen im Labor und atmosphärischem Aerosol durchgeführt. Die Aerosolpartikel bzw. Ice Nuclei IN werden bei Temperaturen unter dem Gefrierpunkt und Übersättigungen in Bezug auf Eis zum Anwachsen zu Eiskristallen gebracht, um sie mittels optischer Detektion zu erfassen. In FINCH ist dies durch das Prinzip der Mischung realisiert, wodurch eine kontinuierliche Messung der IN-Anzahlkonzentration gewährleistet ist. Hierbei kann mit sehr hohen Sammelflussraten von bis zu 10 l/min gemessen werden. Ebenso ist ein schnelles Abfahren von verschiedenen Sättigungsverhältnissen in Bezug auf Eis in einem weiten Bereich von 0.9 - 1.7 bei konstanten Temperaturen bis zu −23 °C möglich. Die Detektion der Eiskristalle und damit der Bestimmung der IN-Anzahlkonzentration erfolgt über einen neu entwickelten optischen Sensor basierend auf der unterschiedlichen Depolarisation des zurückgestreuten Lichtes von Eiskristallen und unterkühlten Tropfen. In Labermessungen wurden Aktivierungstemperatur und -sättigungsverhältnis von Silberjodid AgI und Kaolinit vermessen. Die Resultate zeigten gute Übereinstimmungen mit Ergebnissen aus der Literatur sowie Parallelmessungen mit FRIDGE (FRankfurt Ice Deposition freezinG Experiment). FRIDGE ist eine statische Diffusionskammer zur Aktivierung und Auszählung von Eiskeimen, die auf einem Filter gesammelt wurden. Bei atmosphärischen Messungen auf dem Jungfraujoch(Schweiz) lagen die IN-Anzahlkonzentrationen mit bis zu 4 l−1 im Rahmen der aus der Literatur bekannten Werte. Messungen der Eiskristallresiduen von Mischwolken zeigten hingegen, dass nur jedes tausendste als Eiskeim im Depositionsmode aktiv ist. Hier scheinen andere Gefrierprozesse und sekundäre Eiskristallbildung von sehr großer Bedeutung für die Anzahlkonzentration der Eiskristallresiduen zu sein. Eine weitere Messung von atmosphärischem Aerosol in Frankfurt zeigte IN-Anzahlkonzentrationen bis zu 30 l−1 bei Aktivierungstemperaturen um −14 °C. Die parallele Probenahme auf Siliziumplättchen für die Messungen der IN-Anzahlkonzentration in FRIDGE ergaben Werte im gleichen Anzahlkonzentrationsbereich.

Very high methane uptake on activated carbons prepared from mesophase pitch: A compromise between microporosity and bulk density

Two petroleum residues were pyrolyzed under two different conditions to obtain pitches with low or high mesophase content. The effect of the KOH: precursor ratio and the activation temperature on the packing density and porous texture of the carbons have been studied and optimized. Activated carbons combining high micropore volume (>1 cm3/g) and high packing density (0.7 g/cm3) have been successfully prepared. Regarding excess methane adsorption capacities, the best results (160 cm3 (STP)/cm3 at 25 °C and 3.5 MPa) were obtained using the pitch with the higher content of the more organized mesophase, activated at relatively low temperature (700 °C), with a medium KOH: precursor ratio (3:1). Some of the activated carbons exhibit enhanced adsorption capacity at high pressure, giving values as high as 175 cm3 (STP)/cm3 at 25 °C and 5 MPa and 200 cm3 (STP)/cm3 at 25 °C and 10 MPa (the same amount as in an empty cylinder but at half of the pressure), indicating a contribution of large micropores and narrow mesopores to adsorption at high pressure. The density of methane in pores between 1 and 2.5 nm at pressure up to 10 MPa was estimated to understand their contribution to the total adsorption capacity.

Synthesis of glycerol-based carbon materials as environmental application

Crude glycerol, obtained from the biodiesel production, is actually an abundant and low-cost feedstock, making the preparation of carbonaceous materials by partial carbonization and sulfonation of this by-product an interesting research focus. Bearing this in mind, the aim of this study is to explore several types of glycerol-based carbon materials synthesized by partial carbonization of glycerol in concentrated sulphuric acid solution for the removal of flumequine and tetracycline from aqueous solutions. This study is focused on the synthesis and application of glycerol-based carbon materials as adsorbents for the removal of the antibiotic compounds flumequine and tetracycline from aqueous solution. The different synthesized materials were labelled as GBCM followed by a subscript number corresponding to the activation temperature in oC (i.e., GBCM200, GBCM300, and GBCM350)

Comparison of the effect of pre-treatment and catalysts on liquid quality from fast pyrolysis of biomass

The overall objective of this work was to compare the effect of pre-treatment and catalysts on the quality of liquid products from fast pyrolysis of biomass. This study investigated the upgrading of bio-oil in terms of its quality as a bio-fuel and/or source of chemicals. Bio-oil used directly as a biofuel for heat or power needs to be improved particularly in terms of temperature sensitivity, oxygen content, chemical instability, solid content, and heating values. Chemicals produced from bio-oil need to be able to meet product specifications for market acceptability. There were two main objectives in this research. The first was to examine the influence of pre-treatment of biomass on the fast pyrolysis process and liquid quality. The relationship between the method of pre-treatment of biomass feedstock to fast pyrolysis oil quality was studied. The thermal decomposition behaviour of untreated and pretreated feedstocks was studied by using a TGA (thermogravimetric analysis) and a Py-GC/MS (pyroprobe-gas chromatography/mass spectrometry). Laboratory scale reactors (100g/h, 300g/h, 1kg/h) were used to process untreated and pretreated feedstocks by fast pyrolysis. The second objective was to study the influence of numerous catalysts on fast pyrolysis liquids from wheat straw. The first step applied analytical pyrolysis (Py-GC/MS) to determine which catalysts had an effect on fast pyrolysis liquid, in order to select catalysts for further laboratory fast pyrolysis. The effect of activation, temperature, and biomass pre-treatment on catalysts were also investigated. Laboratory experiments were also conducted using the existing 300g/h fluidised bed reactor system with a secondary catalytic fixed bed reactor. The screening of catalysts showed that CoMo was a highly active catalyst, which particularly reduced the higher molecular weight products of fast pyrolysis. From these screening tests, CoMo catalyst was selected for larger scale laboratory experiments. With reference to the effect of pre-treatment work on fast pyrolysis process, a significant effect occurred on the thermal decomposition of biomass, as well as the pyrolysis products composition, and the proportion of key components in bio-oil. Torrefaction proved to have a mild influence on pyrolysis products, when compared to aquathermolysis and steam pre-treatment.