31 resultados para K2CO3
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Commercial and synthetic mesoporous aluminas impregnated with potassium carbonate were characterized by X-ray diffraction (XRD), nitrogen physisorption, infrared spectroscopy and 27Al MAS NMR. The activities in the transesterification reaction of sunflower oil with methanol for biodiesel production were evaluated. 27Al MAS NMR spectra evidenced the presence of AlIV and AlVI in the samples, and also of AlV sites in the mesoporous synthesized alumina, which disappeared after impregnation with potassium salt followed by calcination. All aluminas containing potassium were active for biodiesel production from sunflower seed oil, with high conversions by both conventional heating and microwave irradiation.
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The activity and selectivity of bi-functional carbon-supported platinum catalysts for the hydroisomerization of n-alkanes have been studied. The influence of the properties of the carbon support on the performance of the catalysts were investigated by incorporating the metallic function on a series of carbons with varied porosity (microporous: GL-50 from Norit, and mesoporous: CMK-3) and surface chemistry (modified by wet oxidation). The characterization results achieved with H-2 chemisorption and TEM showed differences in surface metal concentrations and metal-support interactions depending on the support composition. The highest metal dispersion was achieved after oxidation of the carbon matrix in concentrated nitric acid, suggesting that the presence of surface functional sites distributed in inner and outer surface favors a homogeneous metal distribution. On the other hand, the higher hydrogenating activity of the catalysts prepared with the mesoporous carbon pointed out that a fast molecular traffic inside the pores plays an important role in the catalysts performance. For n-decane hydroisomerization of long chain n-alkanes, higher activities were obtained for the catalysts with an optimized acidity and metal dispersion along with adequate porosity, pointing out the importance of the support properties in the performance of the catalysts.
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Dissertação para obtenção do Grau de Mestre em Engenharia química e bioquímica
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Grande parte dos resíduos de biomassa gerados na indústria agro-alimentar encontram-se subvalorizados. Como tal, é fundamental desenvolver processos capazes de converter esses resíduos em produtos de valor acrescentado. Por outro lado, os compostos farmacêuticos são considerados contaminantes emergentes das águas residuais e com efeitos nocivos para a saúde humana e dos animais. Tendo em conta este enquadramento, resíduos industriais de processamento de batata, foram convertidos em biocarvão activado e utilizados como adsorventes do fármaco Diclofenac, em fase líquida. Os resíduos de biomassa, maioritariamente casca de batata, foram submetidos a caracterização química e a análise termogravimétrica. O biocarvão foi obtido por activação química dos resíduos de biomassa com K2CO3 a 700ºC durante 1 hora, em atmosfera de azoto. Seguidamente foi submetido a caracterização textural e química. O biocarvão (CRB) foi aplicado à remoção de diclofenac sódico (DCF), em fase aquosa, e o seu desempenho foi comparado com o de um carvão activado comercial (GAC). Ambos os carvões, apresentaram-se como materiais microporosos, mas o CRB revelou possuir uma extensa rede macroporosa que se reflectiu numa cinética de adsorção do DCF significativamente mais rápida que a do GAC. Concluiu-se que a cinética de adsorção do DCF com o biocarvão obedecia a um modelo de pseudo 2ªordem e a cinética do GAC se ajustava a um modelo de pseudo 1ª ordem. Apesar do GAC apresentar uma capacidade superior de adsorção no equilíbrio, a sua constante cinética foi inferior à do CRB. No estudo das isotérmicas de adsorção, observou-se que ambos os carvões seguiam o modelo de Langmuir. Apesar da maior capacidade de adsorção do carvão comercial, a constante de Langmuir para o carvão CRB apresentou-se acentuadamente superior, revelando maior afinidade do DCF com este carvão. Para além disso, a cinética superior do CRB representa uma vantagem para processos em que este parâmetro seja determinante.
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O trabalho que se apresenta nesta dissertação foi realizado na Faculdade de Ciências da Universidade de Lisboa, no Grupo de Adsorção e Materiais Adsorventes em parceria com o grupo de Engenharia das Reacções (Departamento de Química, REQUIMTE) da Faculdade de Ciências e Tecnologia da Universidade Nova de Lisboa. De uma parte do trabalho desenvolvido resultaram duas comunicações na Annual World Conference on Carbon 2012 na Cracóvia, Polônia, que se realizou em Junho de 2012; e uma comunicação aceite para apresentação na XXXVII Reunião Ibérica de Adsorção (RIA 2012) em Sevilla, Espanha, que se irá realizar em Setembro de 2012.
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O transporte de nutriente até à superfície das raízes pode ocorrer por fluxo de massa ou por fluxo de massa e difusão, dependendo da atividade do nutriente na solução do solo e da exigência nutricional da planta. Objetivou-se verificar a contribuição dos mecanismos de fluxo de massa e de difusão para o suprimento de potássio, de cálcio e de magnésio a plantas de arroz, em experimento realizado em casa de vegetação. Aplicaram-se em amostra de Latossolo Variação Una, os seguintes tratamentos: Na2CO3, K2CO3, CaCO3 e MgCO3. Aos 75 dias da semeadura, as plantas de arroz foram colhidas e determinadas as quantidades de potássio, de cálcio e de magnésio nelas acumuladas, bem como a concentração desses nutrientes na solução do solo. Essas concentrações, multiplicadas pelo volume de água transpirado, foram usadas para calcular o suprimento por fluxo de massa. A difusão foi estimada por diferença entre a quantidade do nutriente acumulado no vegetal e a transportada por fluxo de massa. Verificou-se que o potássio foi transportado predominantemente por difusão, exceto no tratamento com K2CO3, que gerou altos teores de K na solução de solo, tornando o fluxo de massa suficiente para atender à demanda das plantas. O cálcio e o magnésio foram transportados por fluxo de massa. Segundo os resultados, a difusão foi o principal mecanismo de transporte de potássio nas condições do experimento; todavia, o fluxo de massa pode satisfazer isoladamente a demanda nutricional da planta, quando a concentração de potássio na solução do solo for muito elevada.
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Sulfur in the soil occurs in two basic forms, organic and inorganic S. The organic form accounts for 95 % of S in most soils. The effectiveness of organic S to oxidate to sulfate was evaluated for total S determination in soil samples by wet (acid) and dry-ash (alkaline) oxidation methods. To evaluate the wet method and the possible use as a reference when evaluating the dry method proposed here, a reference standard from the US National Institute of Standards and Technology (NIST) was used (Montana Soil - NIST 2710). The dry-ash oxidation process with alkaline oxidizing agents is one of the simplest oxidation methods of organic S to the sulfate form and was compared with the wet process. The objective of the study was to develop a dry method that would be easy to apply and allow the complete conversion of organic S to sulfate in soil samples and later detection by turbidimetry. The effectiveness of organic S oxidation to sulfate was evaluated by means of three alkaline oxidation mixtures: NaHCO3 + Ag2O, Eschka mixture (17 % Na2CO3, 66 % MgO, and 17 % K2CO3), and NaHCO3 + CuO. The procedure to quantify the sulfate concentration was based on the reaction with barium chloride and turbidimetric detection. Sulfur quantification in the standard sample by the wet method proved adequate, precise and accurate. It should also be pointed out that no significant differences were found (95 % reliability) between the wet and dry processes (NaHCO3 and Ag2O oxidation mixture) in six different Brazilian soils. The proposed dry method can therefore be used in the preparation of soil samples for total S determination.
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The objective of this work was to determine the most appropriated chemical treatment to be used to dry grapes cv. Rubi for raisin production. Drying curves for convective drying with air at 50ºC, in a tray drier, were obtained for grapes submitted to chemical pretreatments with different concentrations of potassium carbonate and olive oil, and different dipping times, according to factorial designs. Convective drying curves were also obtained for grapes pretreated in aqueous suspensions of soybean lecithin, at varied lecithin concentrations and dipping times. Page model was adjusted to the experimental drying curves, and the calculated drying times showed that the best pretreatment consisted in dipping grapes for 2 minutes in a 5% olive oil and 6% K2CO3 emulsion, at 50ºC, which resulted in a drying time close to that of the pretreatment with 2.5% of olive oil, but with a lower consumption of this substance. In addition, the immersion of grapes in an aqueous suspension of 2% soy lecithin, at 50ºC, for 5 minutes, resulted in a total drying time slightly higher than the most effective pretreatment.
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Objectives: αvβ3 integrin is of great interest for tumor targeting because of its high concentration in tumor tissue. It recognizes ligands containing an arginine-glycine-aspartate motif (RGD), and a number of RGD-containing peptides have been developed as PET imaging probes of angiogenesis. We synthesized a series of 18F-labeled cyclic-[RGDfK] peptides for in vivo imaging of αvβ3 expression. Our F-18 labeled prosthetic groups were attached to the αvβ3 ligand via click chemistry, and the reaction conditions (time, temperature, solvent and pH) were optimized by using single modified amino acids.Methods: Seven amino acids were selected considering their different biochemical properties (polarity, total charge, presence of aromatic ring and heteroatom). All the amino acids were modified by the introduction of azido moiety to allow the interaction with alkyne prosthetic groups. Once the conditions of the click chemistry were optimized, the prosthetic groups were also coupled with the cyclic-[RGDfK] exhibiting an azido function. 4- Trimethylammonium-nitrobenzene triflate was used as precursor for the radiosynthesis of the prosthetic groups. The fluorination was carried out with K2CO3/K2.2.2 in CH3CN at 95 oC, and the nitro group was reduced with NaBH4 and Pd/C in MeOH. The resulting 18F-aniline was subsequently coupled to alkynoic acids to yield the final F-18 labeled prosthetic groups. Finally, the prosthetic groups were attached to the peptides via Huisgen's cycloaddition. Figure 1. F-18 labeled αvβ3 ligand.Results: Our new prosthetic groups were successfully clicked to the modified amino acids and to the cyclic- [RGDfK], and the reactions were almost quantitative within 1 to 3.5 h. The pH of the reaction did not influence the reaction kinetic and yield. The four steps of the F-18 labeling were completely automated providing the final products in quantities and yields practical for PET imaging. IC50 values of our ligands for αvβ3 and α5β1 demonstrated a high selectivity of our compounds towards αvβ3, as well as the negligible effect of the prosthetic groups on the affinity of the ligand to its receptor, as confirmed by the prediction of the molecular modeling.Conclusions: We have successfully synthesized novel F-18 labeled prosthetic groups, as well as novel PET imaging probes of αvβ3 expression. The reaction conditions of the Huisgen's cycloaddition were optimized with selected modified amino acids, and subsequently transposed to the cyclic-[RGDfK] peptide. IC50 data demonstrate that our 18F-labeled ligands were selective for αvβ3. In vivo microPET/CT studies in tumor bearing mice are underway.
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Vanadium oxide supported on hydrotalcite-type precursors was studied in the decomposition of isopropanol. Hydrotalcite-type compounds with different y = Mg+2/Al+3 ratios were synthesized by the method of coprecipitating nitrates of Mg+2 and Al+3 cations with K2CO3 as precipitant. The X-ray diffraction patterns of Al-rich hydrotalcite precursors showed the presence of crystalline phases of brucite and gibbsite. It was shown that chemical composition, texture, acid-base properties of the active sites and also Mg/Al ratio strongly affect the formation of the products in the oxidation of isopropanol. The Al-rich catalysts were much more active than the Mg-rich ones, converting isopropanol mainly to propylene.
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The objective of this work is to show the results of the in situ transesterification of sunflower seed oil with methanol on basic homogeneous and heterogeneous catalysis for the production of biodiesel. In homogeneous catalysis, the activity of KOH and K2CO3 were evaluated using the same oil:methanol ratio of 1:90. KOH showed to be more active than K2CO3, leading to total conversion in biodiesel after 1h reaction time. In the heterogeneous catalysis the activity of K2CO3/Al2O3 was comparable to the activity of K2CO3 bulk: 53.0 and 66.6% resp. The properties of samples of biodiesel produced by homogeneous and heterogeneous catalysis were evaluated and are in accordance with the recommended fuel properties.
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The effect of different heterogeneous catalysts on the microwave-assisted transesterification of sunflower oil for the production of methylic biodiesel in a monomode microwave reactor is described. The experiments were carried out at 70 ºC with a 16:1 methanolsunflower oil molar ratio and different heterogeneous basic and acidic catalysts. The results showed that the microwave-heated reactions occur up to four times faster than those carried out with conventional heating. The reactions were performed with 24 catalysts; pure calcium oxide (CaO) and potassium carbonate, either pure or supported by alumina (K2CO3/Al2O3), were the most efficient catalysts.
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The Kraft pulping process is the dominant chemical pulping process in the world. Roughly 195 million metric tons of black liquor are produced annually as a by-product from the Kraft pulping process. Black liquor consists of spent cooking chemicals and dissolved organics from the wood and can contain up to 0.15 wt% nitrogen on dry solids basis. The cooking chemicals from black liquor are recovered in a chemical recovery cycle. Water is evaporated in the first stage of the chemical recovery cycle, so the black liquor has a dry solids content of 65-85% prior to combustion. During combustion of black liquor, a portion of the black liquor nitrogen is volatilized, finally forming N2 or NO. The rest of the nitrogen remains in the char as char nitrogen. During char conversion, fixed carbon is burned off leaving the pulping chemicals as smelt, and the char nitrogen forms mostly smelt nitrogen (cyanate, OCN-). Smelt exits the recovery boiler and is dissolved in water. The cyanate from smelt decomposes in the presence of water, forming NH3, which causes nitrogen emissions from the rest of the chemical recovery cycle. This thesis had two focuses: firstly, to determine how the nitrogen chemistry in the recovery boiler is affected by modification of black liquor; and secondly, to find out what causes cyanate formation during thermal conversion, and which parameters affect cyanate formation and decomposition during thermal conversion of black liquor. The fate of added biosludge nitrogen in chemical recovery was determined in Paper I. The added biosludge increased the nitrogen content of black liquor. At the pulp mill, the added biosludge did not increase the NO formation in the recovery boiler, but instead increased the amount of cyanate in green liquor. The increased cyanate caused more NH3 formation, which increased the NCG boiler’s NO emissions. Laboratory-scale experiments showed an increase in both NO and cyanate formation after biosludge addition. Black liquor can be modified, for example by addition of a solid biomass to increase the energy density of black liquor, or by separation of lignin from black liquor by precipitation. The precipitated lignin can be utilized in the production of green chemicals or as a fuel. In Papers II and III, laboratory-scale experiments were conducted to determine the impact of black liquor modification on NO and cyanate formation. Removal of lignin from black liquor reduced the nitrogen content of the black liquor. In most cases NO and cyanate formation decreased with increasing lignin removal; the exception was NO formation from lignin lean soda liquors. The addition of biomass to black liquor resulted in a higher nitrogen content fuel mixture, due to the higher nitrogen content of biomass compared to black liquor. More NO and cyanate were formed from the fuel mixtures than from pure black liquor. The increased amount of formed cyanate led to the hypothesis that black liquor is catalytically active and converts a portion of the nitrogen in the mixed fuel to cyanate. The mechanism behind cyanate formation during thermal conversion of black liquor was not clear before this thesis. Paper IV studies the cyanate formation of alkali metal loaded fuels during gasification in a CO2 atmosphere. The salts K2CO3, Na2CO3, and K2SO4 all promoted char nitrogen to cyanate conversion during gasification, while KCl and CaCO3 did not. It is now assumed that cyanate is formed when alkali metal carbonate or an active intermediate of alkali metal carbonate (e.g. -CO2K) reacts with the char nitrogen forming cyanate. By testing different fuels (bark, peat, and coal), each of which had a different form of organic nitrogen, it was concluded that the form of organic nitrogen in char also has an impact on cyanate formation. Cyanate can be formed during pyrolysis of black liquor, but at temperatures 900°C or above, the formed cyanate will decompose. Cyanate formation in gasifying conditions with different levels of CO2 in the atmosphere was also studied. Most of the char nitrogen was converted to cyanate during gasification at 800-900°C in 13-50% CO2 in N2, and only 5% of the initial fuel nitrogen was converted to NO during char conversion. The formed smelt cyanate was stable at 800°C 13% CO2, while it decomposed at 900°C 13% CO2. The cyanate decomposition was faster at higher temperatures and in oxygen-containing atmospheres than in an inert atmosphere. The presence of CO2 in oxygencontaining atmospheres slowed down the decomposition of cyanate. This work will provide new information on how modification of black liquor affects the nitrogen chemistry during thermal conversion of black liquor and what causes cyanate formation during thermal conversion of black liquor. The formation and decomposition of cyanate was studied in order to provide new data, which would be useful in modeling of nitrogen chemistry in the recovery boiler.
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A Análise Descritiva Quantitativa(ADQ) foi empregada para caracterização das amostras de pós de cacau que representaram a amplitude do delineamento composto rotacional central 2 do processo de alcalinização dos "nibs" de cacau. As variáveis independentes foram faixas de temperatura de 60 a 120 ºC, de tempo de 30 a 150min e de concentração de K2CO3 de 1,22 a 4,78%. Foram avaliadas oito amostras de pó de cacau representativas das variações de cor e aceitabilidade do total das amostras obtidas experimentalmente e duas amostras de marcas comerciais. A análise do aroma foi feita diretamente nos pós de cacau alcalinizados e a dos demais atributos na forma de bebida achocolatada (2% do pó de cacau e 7% de açúcar em leite desnatado esterilizado). Doze provadores selecionados com base no seu poder de discriminação, reprodutibilidade e concordância com a equipe geraram em consenso, pelo método de rede (Kelly's Repertory Grid Method), três termos descritos para o aroma (alcalino, chocolate e queimado) e doze para os achocolatados (solubilidade, marrom, marrom avermelhado, chocolate, queimado, caramelo, doce, adstringente, alcalino, amargo, salgado e corpo). As avaliações das amostras foram feitas monadicamente com três repetições e em cabines individuais. Os dados obtidos foram submetidos a ANOVA, teste de Tukey e Análise de Componentes Principais. As avaliações dos aromas dos pós de cacau mostraram relação direta entre o aroma alcalino e os teores de álcali, temperatura e tempo do processo. De modo geral, os produtos com menores concentrações de K2CO3 (1,22 - 3,00% ) apresentaram aroma e sabor de chocolate mais fortes. Encontrou-se uma relação direta entre os teores de álcali no produto e o sabor alcalino, queimado e adstringente e uma relação inversa com a luminosidade da cor. Assim, as amostras com maior concentração de K2CO3 (4,78%), foram consideradas pela equipe sensorial, as de mais forte sabor e aroma alcalino, queimado e adstringente, assim como de cor marrom e marrom avermelhado mais escura. Todos os processos levaram à obtenção de amostras com alta solubilidade e fraco sabor amargo.
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This thesis is divided in to 9 chapters and deals with the modification of TiO2 for various applications include photocatalysis, thermal reaction, photovoltaics and non-linear optics. Chapter 1 involves a brief introduction of the topic of study. An introduction to the applications of modified titania systems in various fields are discussed concisely. Scope and objectives of the present work are also discussed in this chapter. Chapter 2 explains the strategy adopted for the synthesis of metal, nonmetal co-doped TiO2 systems. Hydrothermal technique was employed for the preparation of the co-doped TiO2 system, where Ti[OCH(CH3)2]4, urea and metal nitrates were used as the sources for TiO2, N and metals respectively. In all the co-doped systems, urea to Ti[OCH(CH3)2]4 was taken in a 1:1 molar ratio and varied the concentration of metals. Five different co-doped catalytic systems and for each catalysts, three versions were prepared by varying the concentration of metals. A brief explanation of physico-chemical techniques used for the characterization of the material was also presented in this chapter. This includes X-ray Diffraction (XRD), Raman Spectroscopy, FTIR analysis, Thermo Gravimetric Analysis, Energy Dispersive X-ray Analysis (EDX), Scanning Electron Microscopy(SEM), UV-Visible Diffuse Reflectance Spectroscopy (UV-Vis DRS), Transmission Electron Microscopy (TEM), BET Surface Area Measurements and X-ray Photoelectron Spectroscopy (XPS). Chapter 3 contains the results and discussion of characterization techniques used for analyzing the prepared systems. Characterization is an inevitable part of materials research. Determination of physico-chemical properties of the prepared materials using suitable characterization techniques is very crucial to find its exact field of application. It is clear from the XRD pattern that photocatalytically active anatase phase dominates in the calcined samples with peaks at 2θ values around 25.4°, 38°, 48.1°, 55.2° and 62.7° corresponding to (101), (004), (200), (211) and (204) crystal planes (JCPDS 21-1272) respectively. But in the case of Pr-N-Ti sample, a new peak was observed at 2θ = 30.8° corresponding to the (121) plane of the polymorph brookite. There are no visible peaks corresponding to dopants, which may be due to their low concentration or it is an indication of the better dispersion of impurities in the TiO2. Crystallite size of the sample was calculated from Scherrer equation byusing full width at half maximum (FWHM) of the (101) peak of the anatase phase. Crystallite size of all the co-doped TiO2 was found to be lower than that of bare TiO2 which indicates that the doping of metal ions having higher ionic radius into the lattice of TiO2 causes some lattice distortion which suppress the growth of TiO2 nanoparticles. The structural identity of the prepared system obtained from XRD pattern is further confirmed by Raman spectra measurements. Anatase has six Raman active modes. Band gap of the co-doped system was calculated using Kubelka-Munk equation and that was found to be lower than pure TiO2. Stability of the prepared systems was understood from thermo gravimetric analysis. FT-IR was performed to understand the functional groups as well as to study the surface changes occurred during modification. EDX was used to determine the impurities present in the system. The EDX spectra of all the co-doped samples show signals directly related to the dopants. Spectra of all the co-doped systems contain O and Ti as the main components with low concentrations of doped elements. Morphologies of the prepared systems were obtained from SEM and TEM analysis. Average particle size of the systems was drawn from histogram data. Electronic structures of the samples were identified perfectly from XPS measurements. Chapter 4 describes the photocatalytic degradation of herbicides Atrazine and Metolachlor using metal, non-metal co-doped titania systems. The percentage of degradation was analyzed by HPLC technique. Parameters such as effect of different catalysts, effect of time, effect of catalysts amount and reusability studies were discussed. Chapter 5 deals with the photo-oxidation of some anthracene derivatives by co-doped catalytic systems. These anthracene derivatives come underthe category of polycyclic aromatic hydrocarbons (PAH). Due to the presence of stable benzene rings, most of the PAH show strong inhibition towards biological degradation and the common methods employed for their removal. According to environmental protection agency, most of the PAH are highly toxic in nature. TiO2 photochemistry has been extensively investigated as a method for the catalytic conversion of such organic compounds, highlighting the potential of thereof in the green chemistry. There are actually two methods for the removal of pollutants from the ecosystem. Complete mineralization is the one way to remove pollutants. Conversion of toxic compounds to another compound having toxicity less than the initial starting compound is the second way. Here in this chapter, we are concentrating on the second aspect. The catalysts used were Gd(1wt%)-N-Ti, Pd(1wt%)-N-Ti and Ag(1wt%)-N-Ti. Here we were very successfully converted all the PAH to anthraquinone, a compound having diverse applications in industrial as well as medical fields. Substitution of 10th position of desired PAH by phenyl ring reduces the feasibility of photo reaction and produced 9-hydroxy 9-phenyl anthrone (9H9PA) as an intermediate species. The products were separated and purified by column chromatography using 70:30 hexane/DCM mixtures as the mobile phase and the resultant products were characterized thoroughly by 1H NMR, IR spectroscopy and GCMS analysis. Chapter 6 elucidates the heterogeneous Suzuki coupling reaction by Cu/Pd bimetallic supported on TiO2. Sol-Gel followed by impregnation method was adopted for the synthesis of Cu/Pd-TiO2. The prepared system was characterized by XRD, TG-DTG, SEM, EDX, BET Surface area and XPS. The product was separated and purified by column chromatography using hexane as the mobile phase. Maximum isolated yield of biphenyl of around72% was obtained in DMF using Cu(2wt%)-Pd(4wt%)-Ti as the catalyst. In this reaction, effective solvent, base and catalyst were found to be DMF, K2CO3 and Cu(2wt%)-Pd(4wt%)-Ti respectively. Chapter 7 gives an idea about the photovoltaic (PV) applications of TiO2 based thin films. Due to energy crisis, the whole world is looking for a new sustainable energy source. Harnessing solar energy is one of the most promising ways to tackle this issue. The present dominant photovoltaic (PV) technologies are based on inorganic materials. But the high material, low power conversion efficiency and manufacturing cost limits its popularization. A lot of research has been conducted towards the development of low-cost PV technologies, of which organic photovoltaic (OPV) devices are one of the promising. Here two TiO2 thin films having different thickness were prepared by spin coating technique. The prepared films were characterized by XRD, AFM and conductivity measurements. The thickness of the films was measured by Stylus Profiler. This chapter mainly concentrated on the fabrication of an inverted hetero junction solar cell using conducting polymer MEH-PPV as photo active layer. Here TiO2 was used as the electron transport layer. Thin films of MEH-PPV were also prepared using spin coating technique. Two fullerene derivatives such as PCBM and ICBA were introduced into the device in order to improve the power conversion efficiency. Effective charge transfer between the conducting polymer and ICBA were understood from fluorescence quenching studies. The fabricated Inverted hetero junction exhibited maximum power conversion efficiency of 0.22% with ICBA as the acceptor molecule. Chapter 8 narrates the third order order nonlinear optical properties of bare and noble metal modified TiO2 thin films. Thin films were fabricatedby spray pyrolysis technique. Sol-Gel derived Ti[OCH(CH3)2]4 in CH3CH2OH/CH3COOH was used as the precursor for TiO2. The precursors used for Au, Ag and Pd were the aqueous solutions of HAuCl4, AgNO3 and Pd(NO3)2 respectively. The prepared films were characterized by XRD, SEM and EDX. The nonlinear optical properties of the prepared materials were investigated by Z-Scan technique comprising of Nd-YAG laser (532 nm,7 ns and10 Hz). The non-linear coefficients were obtained by fitting the experimental Z-Scan plot with the theoretical plots. Nonlinear absorption is a phenomenon defined as a nonlinear change (increase or decrease) in absorption with increasing of intensity. This can be mainly divided into two types: saturable absorption (SA) and reverse saturable absorption (RSA). Depending on the pump intensity and on the absorption cross- section at the excitation wavelength, most molecules show non- linear absorption. With increasing intensity, if the excited states show saturation owing to their long lifetimes, the transmission will show SA characteristics. Here absorption decreases with increase of intensity. If, however, the excited state has strong absorption compared with that of the ground state, the transmission will show RSA characteristics. Here in our work most of the materials show SA behavior and some materials exhibited RSA behavior. Both these properties purely depend on the nature of the materials and alignment of energy states within them. Both these SA and RSA have got immense applications in electronic devices. The important results obtained from various studies are presented in chapter 9.