962 resultados para Pulsed fluid bed dryer


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The construction of wells is one of the most important activities of the oil industry. The drilling process is the set of activities and operations to design, program and perform the opening thereof. During this process, the cuttings are removed by the drilling fluid, or mud, and carted to the surface. This fluid is injected into the drill string and returns to the surface through the annular space between the well walls and the drill string. After the descent of the column casing, the annular space between the casing string and the walls of the borehole is filled with cement so as to secure the spine and prevent any migration of fluids between the various permeable zones traversed by the well behind of the coating. To ensure the good quality of the cementation scrubbers are used mattresses which are pumped ahead of the cement slurry so as to avoid contamination of the drilling fluid paste, or vice versa, and assist in the removal of plaster, formed by drilling fluid of the borehole walls, thus enabling a better cement bond to the well. Within this context, this work aims to evaluate the efficiency of mattresses scrubbers, the basis of ionic and nonionic surfactants, on the removal of nonaqueous drilling fluid, based on n-paraffin in oil wells, and the compatibility between the Mattress relations washer / drilling fluid bed scrubber / cement paste mattress washer / cement slurry / drilling fluid and the drilling fluid / cement slurry using laboratory tests rheology, thickening time and compressive strength. Also technique was performed X-ray diffraction (XRD) for a more detailed analysis of these mixtures with hydrated cement paste. In compatibility tests the conditions of temperature and pressure used in the same laboratory procedure simulating the conditions of oil wells, the well is considered the depth of 800 m. The results showed that the compositions of the mattress washer nonionic, KMS obtained a 100% efficient in removing the non-aqueous drilling fluid, and the best formulation showed good results with respect to compliance testing

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Fresh persimmon has a high moisture content (about 85% wet basis) making it highly perishable and requiring adequate drying conditions to obtain an acceptable dehydrated product. Drying kinetics of persimmon cv. Rama Forte was studied in a fixed bed dryer at temperatures ranging from 50 to 80 degreesC and air velocity of 0.8 m/s. Shrinkage during drying was described by a linear correlation with respect to water content. Evaluation of effective diffusivity as a function of moisture content, with undergoing shrinkage during drying was based on Fourier series solution of Fick's diffusion equation. Effective diffusivity values at moisture contents between 0.09 - 4.23 kg water/kg dry matter were found to be in the range of 2.6 x 10(-10) m(2)/s to 5.4 x 10(-10) m(2)/s, and its dependence on air drying temperature was represented by an Arrhenius type equation. Activation energy increased with decreasing water content in persimmons.

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Pós-graduação em Engenharia e Ciência de Alimentos - IBILCE

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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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De origem asiática, a semente de linhaça (Linum usitatissimum L.) pertence à família das Lináceas e é obtida a partir do linho. A semente da linhaça é ainda a maior fonte alimentar de lignanas, compostos fotoquímicos parecidos com o estrogênio, que podem desempenhar ação anticancerígena. Rica em fibras solúveis tem aproximadamente 40% do seu peso composto por óleos ricos em Ômega 3, entre os quais se destaca o α-linolênico. A secagem é a operação unitária segundo o qual ocorre eliminação da água por evaporação ou sublimação, presente em um material, mediante a aplicação de calor com condições controladas. Visando averiguar o comportamento das sementes de linhaça durante a operação de secagem, o presente trabalho teve como objetivo principal realizar o planejamento experimental e analisar estatísticamente os resultados empregados para quantificar a influência da temperatura do ar (T), tempo de secagem (t), velocidade do ar de fluidização (Uf) e carga de sólidos (Cs), sobre a razão de umidade (Xr), rendimento em óleo (Rend.) e os parâmetros oleoquimicos. A estimativa do ponto ótimo de operação foi determinada em função das variáveis de entrada aplicando o conceito de desejabilidade global. Dentre as condições estabelecidas neste trabalho, o valor ótimo da Função Desejabilidade é quando T é deslocada próximo ao nível alto (72 oC), t para o mínimo (3 h), Uf para o ponto próximo ao central (0,83 m/s) e a Cs para o nível alto (500g), obtendo-se assim: 0,126 para Xr; 36,92 % para Rend.; 4,51 mg KOH/g para IA; 22,52 meqO2/Kg IP e 0,31% para DC. Foram obtidas as isotermas de dessorção das sementes de linhaça nas temperaturas de 40, 60 e 80°C. Os dados experimentais foram avaliados usando seis modelos matemáticos. A entalpia e a entropia diferencial de dessorção foram estimadas por meio das relações de Clausius-Clapeyron e Gibbs-Helmholtz, respectivamente. Os modelos de GAB e Peleg ajustaram adequadamente os dados experimentais. A teoria da compensação entalpia-entropia foi aplicada com sucesso às isotermas de dessorção e indica que o mecanismo de dessorção de umidade das sementes de linhaça pode ser considerado como controlado pela entalpia. A secagem das sementes de linhaça previamente umidificadas foram avaliadas em um secador de leito fixo e fluidizado, as corridas experimentais foram realizadas nas temperaturas de 40, 60 e 80°C, dentre dos cinco modelos propostos, o modelo de Midilli et al, foi o melhor modelo que melhor ajustou aos dados experimentais. Foi observado que a difusividade efetiva para as sementes de linhaça aumentou com a elevação da temperatura do ar de secagem para a secagem em leito fixo e fluidizado. A dependência da difusividade em relação à temperatura foi descrita pela equação de Arrhenius, por meio da qual se estimou para ambos os processos de secagem.

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Este estudo avaliou a composição química da farinha de banana verde sem casca e com casca, obtido por secagem em leito de jorro, com o objetivo de agregar valor nutricional a produtos alimentícios. As bananas foram cortadas e trituradas para a obtenção de uma pasta, sendo esta alimentada no secador leito de jorro (12 cm de altura e T = 80 º C), a fim de obter uma farinha. As farinhas obtidas foram submetidas a análise da umidade, proteína, cinzas, Carboidratos totais, amido total, amido resistente, e fibras. As farinhas de banana verde, principalmente com casca, são boas fontes de fibras e amido resistente, com uma média de 21,91g/100g e 68,02g/100g respectivamente. O teor médio de proteína encontrado foi para 4,76g/100g, sendo classificada como uma proteína de baixo valor biológico, tendo a lisina como o primeiro aminoácido limitante. Os resultados mostraram que a farinha de banana verde com casca obtida por secagem em leito de jorro pode ser uma ferramenta valiosa para agregação de valor nutricional aos produtos, a fim de aumentar a sua fracção não digerível.

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Pós-graduação em Agronomia (Energia na Agricultura) - FCA

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The effect of ultrasound and osmotic dehydration pretreatments on papaya drying kinetics was investigated. The ultrasound pretreatment was carried out in an ultrasonic bath at 30 A degrees C. The osmotic pretreatment in sucrose solution was carried out in an incubator at 34 A degrees C and agitation of 80 rpm for 210 min. The drying process was conducted in a fixed bed dryer at 70 A degrees C. Experimental data were fitted successfully using the Page model for dried fresh and pretreated fruits, with coefficient of determination greater than 0.9992 and average relative error lower that 14.4 %. The diffusional model was used to describe the moisture transfer, and the effective water diffusivity was identified in the order of 10(-9) m(2) s(-1). It was found that drying rates of osmosed fruits were the lowest due to the presence of infused solutes, while the ultrasound pretreatment contributed to faster drying rates. Evaluation of the dried fruit was performed by means of total carotenoids retention. Ultrasound treatments in distilled water prior to air-drying gave rise to dried papayas with retention of carotenoids in the range 30.4-39.8 % and the ultrasonic-assisted osmotic dehydration of papayas showed carotenoids retention values up to 64.9 %, whereas the dried fruit without pretreatment showed carotenoids retention lower than 24 %.

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With the purpose of evaluating the behavior of different polymers employed as binders in small-diameter pellets for oral administration, we prepared formulations containing paracetamol and one of the following polymers: PVP, PEG 1500, hydroxypropylmethylcellulose and methylcellulose, and we evaluated their different binding properties. The pellets were obtained by the extrusion/spheronization process and were subsequently subjected to fluid bed drying. In order to assess drug delivery, the United States Pharmacopeia (USP) apparatus 3 (Bio-Dis) was employed, in conjunction with the method described by the same pharmacopeia for the dissolution of paracetamol tablets (apparatus 1). The pellets were also evaluated for granulometry, friability, true density and drug content. The results indicate that the different binders used are capable of affecting production in different ways, and some of the physicochemical characteristics of the pellets, as well as the dissolution test, revealed that the formulations acted like immediate-release products. The pellets obtained presented favorable release characteristics for orally disintegrating tablets. USP apparatus 3 seems to be more adequate for discriminating among formulations than the basket method.

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Selective oxidation is one of the simplest functionalization methods and essentially all monomers used in manufacturing artificial fibers and plastics are obtained by catalytic oxidation processes. Formally, oxidation is considered as an increase in the oxidation number of the carbon atoms, then reactions such as dehydrogenation, ammoxidation, cyclization or chlorination are all oxidation reactions. In this field, most of processes for the synthesis of important chemicals used vanadium oxide-based catalysts. These catalytic systems are used either in the form of multicomponent mixed oxides and oxysalts, e.g., in the oxidation of n-butane (V/P/O) and of benzene (supported V/Mo/O) to maleic anhydride, or in the form of supported metal oxide, e.g., in the manufacture of phthalic anhydride by o-xylene oxidation, of sulphuric acid by oxidation of SO2, in the reduction of NOx with ammonia and in the ammoxidation of alkyl aromatics. In addition, supported vanadia catalysts have also been investigated for the oxidative dehydrogenation of alkanes to olefins , oxidation of pentane to maleic anhydride and the selective oxidation of methanol to formaldehyde or methyl formate [1]. During my PhD I focused my work on two gas phase selective oxidation reactions. The work was done at the Department of Industrial Chemistry and Materials (University of Bologna) in collaboration with Polynt SpA. Polynt is a leader company in the development, production and marketing of catalysts for gas-phase oxidation. In particular, I studied the catalytic system for n-butane oxidation to maleic anhydride (fluid bed technology) and for o-xylene oxidation to phthalic anhydride. Both reactions are catalyzed by systems based on vanadium, but catalysts are completely different. Part A is dedicated to the study of V/P/O catalyst for n-butane selective oxidation, while in the Part B the results of an investigation on TiO2-supported V2O5, catalyst for o-xylene oxidation are showed. In Part A, a general introduction about the importance of maleic anhydride, its uses, the industrial processes and the catalytic system are reported. The reaction is the only industrial direct oxidation of paraffins to a chemical intermediate. It is produced by n-butane oxidation either using fixed bed and fluid bed technology; in both cases the catalyst is the vanadyl pyrophosphate (VPP). Notwithstanding the good performances, the yield value didn’t exceed 60% and the system is continuously studied to improve activity and selectivity. The main open problem is the understanding of the real active phase working under reaction conditions. Several articles deal with the role of different crystalline and/or amorphous vanadium/phosphorous (VPO) compounds. In all cases, bulk VPP is assumed to constitute the core of the active phase, while two different hypotheses have been formulated concerning the catalytic surface. In one case the development of surface amorphous layers that play a direct role in the reaction is described, in the second case specific planes of crystalline VPP are assumed to contribute to the reaction pattern, and the redox process occurs reversibly between VPP and VOPO4. Both hypotheses are supported also by in-situ characterization techniques, but the experiments were performed with different catalysts and probably under slightly different working conditions. Due to complexity of the system, these differences could be the cause of the contradictions present in literature. Supposing that a key role could be played by P/V ratio, I prepared, characterized and tested two samples with different P/V ratio. Transformation occurring on catalytic surfaces under different conditions of temperature and gas-phase composition were studied by means of in-situ Raman spectroscopy, trying to investigate the changes that VPP undergoes during reaction. The goal is to understand which kind of compound constituting the catalyst surface is the most active and selective for butane oxidation reaction, and also which features the catalyst should possess to ensure the development of this surface (e.g. catalyst composition). On the basis of results from this study, it could be possible to project a new catalyst more active and selective with respect to the present ones. In fact, the second topic investigated is the possibility to reproduce the surface active layer of VPP onto a support. In general, supportation is a way to improve mechanical features of the catalysts and to overcome problems such as possible development of local hot spot temperatures, which could cause a decrease of selectivity at high conversion, and high costs of catalyst. In literature it is possible to find different works dealing with the development of supported catalysts, but in general intrinsic characteristics of VPP are worsened due to the chemical interaction between active phase and support. Moreover all these works deal with the supportation of VPP; on the contrary, my work is an attempt to build-up a V/P/O active layer on the surface of a zirconia support by thermal treatment of a precursor obtained by impregnation of a V5+ salt and of H3PO4. In-situ Raman analysis during the thermal treatment, as well as reactivity tests are used to investigate the parameters that may influence the generation of the active phase. Part B is devoted to the study of o-xylene oxidation of phthalic anhydride; industrially, the reaction is carried out in gas-phase using as catalysts a supported system formed by V2O5 on TiO2. The V/Ti/O system is quite complex; different vanadium species could be present on the titania surface, as a function of the vanadium content and of the titania surface area: (i) V species which is chemically bound to the support via oxo bridges (isolated V in octahedral or tetrahedral coordination, depending on the hydration degree), (ii) a polymeric species spread over titania, and (iii) bulk vanadium oxide, either amorphous or crystalline. The different species could have different catalytic properties therefore changing the relative amount of V species can be a way to optimize the catalytic performances of the system. For this reason, samples containing increasing amount of vanadium were prepared and tested in the oxidation of o-xylene, with the aim of find a correlations between V/Ti/O catalytic activity and the amount of the different vanadium species. The second part deals with the role of a gas-phase promoter. Catalytic surface can change under working conditions; the high temperatures and a different gas-phase composition could have an effect also on the formation of different V species. Furthermore, in the industrial practice, the vanadium oxide-based catalysts need the addition of gas-phase promoters in the feed stream, that although do not have a direct role in the reaction stoichiometry, when present leads to considerable improvement of catalytic performance. Starting point of my investigation is the possibility that steam, a component always present in oxidation reactions environment, could cause changes in the nature of catalytic surface under reaction conditions. For this reason, the dynamic phenomena occurring at the surface of a 7wt% V2O5 on TiO2 catalyst in the presence of steam is investigated by means of Raman spectroscopy. Moreover a correlation between the amount of the different vanadium species and catalytic performances have been searched. Finally, the role of dopants has been studied. The industrial V/Ti/O system contains several dopants; the nature and the relative amount of promoters may vary depending on catalyst supplier and on the technology employed for the process, either a single-bed or a multi-layer catalytic fixed-bed. Promoters have a quite remarkable effect on both activity and selectivity to phthalic anhydride. Their role is crucial, and the proper control of the relative amount of each component is fundamental for the process performance. Furthermore, it can not be excluded that the same promoter may play different role depending on reaction conditions (T, composition of gas phase..). The reaction network of phthalic anhydride formation is very complex and includes several parallel and consecutive reactions; for this reason a proper understanding of the role of each dopant cannot be separated from the analysis of the reaction scheme. One of the most important promoters at industrial level, which is always present in the catalytic formulations is Cs. It is known that Cs plays an important role on selectivity to phthalic anhydride, but the reasons of this phenomenon are not really clear. Therefore the effect of Cs on the reaction scheme has been investigated at two different temperature with the aim of evidencing in which step of the reaction network this promoter plays its role.

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In der Herstellung fester Darreichungsformen umfasst die Granulierung einen komplexen Teilprozess mit hoher Relevanz für die Qualität des pharmazeutischen Produktes. Die Wirbelschichtgranulierung ist ein spezielles Granulierverfahren, welches die Teilprozesse Mischen, Agglomerieren und Trocknen in einem Gerät vereint. Durch die Kombination mehrerer Prozessstufen unterliegt gerade dieses Verfahren besonderen Anforderungen an ein umfassendes Prozessverständnis. Durch die konsequente Verfolgung des PAT- Ansatzes, welcher im Jahre 2004 durch die amerikanische Zulassungsbehörde (FDA) als Guideline veröffentlicht wurde, wurde der Grundstein für eine kontinuierliche Prozessverbesserung durch erhöhtes Prozessverständnis, für Qualitätserhöhung und Kostenreduktion gegeben. Die vorliegende Arbeit befasste sich mit der Optimierung der Wirbelschicht-Granulationsprozesse von zwei prozesssensiblen Arzneistoffformulierungen, unter Verwendung von PAT. rnFür die Enalapril- Formulierung, einer niedrig dosierten und hochaktiven Arzneistoffrezeptur, wurde herausgefunden, dass durch eine feinere Zerstäubung der Granulierflüssigkeit deutlich größere Granulatkörnchen erhalten werden. Eine Erhöhung der MassRatio verringert die Tröpfchengröße, dies führt zu größeren Granulaten. Sollen Enalapril- Granulate mit einem gewünschten D50-Kornverteilung zwischen 100 und 140 um hergestellt werden, dann muss die MassRatio auf hohem Niveau eingestellt werden. Sollen Enalapril- Granulate mit einem D50- Wert zwischen 80 und 120µm erhalten werden, so muss die MassRatio auf niedrigem Niveau eingestellt sein. Anhand der durchgeführten Untersuchungen konnte gezeigt werden, dass die MassRatio ein wichtiger Parameter ist und zur Steuerung der Partikelgröße der Enalapril- Granulate eingesetzt werden kann; unter der Voraussetzung dass alle anderen Prozessparameter konstant gehalten werden.rnDie Betrachtung der Schnittmengenplots gibt die Möglichkeit geeignete Einstellungen der Prozessparameter bzw. Einflussgrößen zu bestimmen, welche dann zu den gewünschten Granulat- und Tabletteneigenschaften führen. Anhand der Lage und der Größe der Schnittmenge können die Grenzen der Prozessparameter zur Herstellung der Enalapril- Granulate bestimmt werden. Werden die Grenzen bzw. der „Design Space“ der Prozessparameter eingehalten, kann eine hochwertige Produktqualität garantiert werden. rnUm qualitativ hochwertige Enalapril Tabletten mit der gewählten Formulierung herzustellen, sollte die Enalapril- Granulation mit folgenden Prozessparametern durchgeführt werden: niedrige Sprührate, hoher MassRatio, einer Zulufttemperatur von mindestens > 50 °C und einer effektiven Zuluftmenge < 180 Nm³/h. Wird hingegen eine Sprührate von 45 g/min und eine mittlere MassRatio von 4.54 eingestellt, so muss die effektive Zuluftmenge mindestens 200 Nm³/h und die Zulufttemperatur mindestens 60 °C betragen, um eine vorhersagbar hohe Tablettenqualität zu erhalten. Qualität wird in das Arzneimittel bereits während der Herstellung implementiert, indem die Prozessparameter bei der Enalapril- Granulierung innerhalb des „Design Space“ gehalten werden.rnFür die Metformin- Formulierung, einer hoch dosierten aber wenig aktiven Arzneistoffrezeptur wurde herausgefunden, dass sich der Wachstumsmechanismus des Feinanteils der Metformin- Granulate von dem Wachstumsmechanismus der D50- und D90- Kornverteilung unterscheidet. Der Wachstumsmechanismus der Granulate ist abhängig von der Partikelbenetzung durch die versprühten Flüssigkeitströpfchen und vom Größenverhältnis von Partikel zu Sprühtröpfchen. Der Einfluss der MassRatio ist für die D10- Kornverteilung der Granulate vernachlässigbar klein. rnMit Hilfe der Störgrößen- Untersuchungen konnte eine Regeleffizienz der Prozessparameter für eine niedrig dosierte (Enalapril)- und eine hoch dosierte (Metformin) Arzneistoffformulierung erarbeitet werden, wodurch eine weitgehende Automatisierung zur Verringerung von Fehlerquellen durch Nachregelung der Störgrößen ermöglicht wird. Es ergibt sich für die gesamte Prozesskette ein in sich geschlossener PAT- Ansatz. Die Prozessparameter Sprührate und Zuluftmenge erwiesen sich als am besten geeignet. Die Nachregelung mit dem Parameter Zulufttemperatur erwies sich als träge. rnFerner wurden in der Arbeit Herstellverfahren für Granulate und Tabletten für zwei prozesssensible Wirkstoffe entwickelt. Die Robustheit der Herstellverfahren gegenüber Störgrößen konnte demonstriert werden, wodurch die Voraussetzungen für eine Echtzeitfreigabe gemäß dem PAT- Gedanken geschaffen sind. Die Kontrolle der Qualität des Produkts findet nicht am Ende der Produktions- Prozesskette statt, sondern die Kontrolle wird bereits während des Prozesses durchgeführt und basiert auf einem besseren Verständnis des Produktes und des Prozesses. Außerdem wurde durch die konsequente Verfolgung des PAT- Ansatzes die Möglichkeit zur kontinuierlichen Prozessverbesserung, zur Qualitätserhöhung und Kostenreduktion gegeben und damit das ganzheitliche Ziel des PAT- Gedankens erreicht und verwirklicht.rn

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Palbio (PAL, Palbio 50 RD, Bioibérica, Spain) is a protein concentrate based on hydrolyzed porcine digestive mucosa dried under a fluid bed system over a soybean carrier, currently used in piglet feeds. The digestibility of PAL is very high and the product may be an excellent source of protein for young chicks. An experiment was conducted with 1,280 straight-run one-d-old Ross 308 chicks to evaluate the growth response of broilers to dietary inclusion of PAL.

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Actualmente, la reducción de materias activas (UE) y la implantación de la nueva Directiva comunitaria 2009/128/ que establece el marco de actuación para conseguir un uso sostenible de los plaguicidas químicos y la preferencia de uso de métodos biológicos, físicos y otros no químicos, obliga a buscar métodos de control menos perjudiciales para el medio ambiente. El control biológico (CB) de enfermedades vegetales empleando agentes de control biológico (ACB) se percibe como una alternativa más segura y con menor impacto ambiental, bien solos o bien como parte de una estrategia de control integrado. El aislado 212 de Penicillium oxalicum (PO212) (ATCC 201888) fue aislado originalmente de la micoflora del suelo en España y ha demostrado ser un eficaz ACB frente a la marchitez vascular del tomate. Una vez identificado y caracterizado el ACB se inició el periodo de desarrollo del mismo poniendo a punto un método de producción en masa de sus conidias. Tras lo cual se inició el proceso de formulación del ACB deshidratando las conidias para su preservación durante un período de tiempo mayor mediante lecho fluido. Finalmente, se han desarrollado algunos formulados que contienen de forma individual diferentes aditivos que han alargado su viabilidad, estabilidad y facilitado su manejo y aplicación. Sin embargo, es necesario seguir trabajando en la mejora de su eficacia de biocontrol. El primer objetivo de esta Tesis se ha centrado en el estudio de la interacción ACB-patógeno-huésped que permita la actuación de P.oxalicum en diferentes patosistemas. Uno de los primeros puntos que se abordan dentro de este objetivo es el desarrollo de nuevas FORMULACIONES del ACB que incrementen su eficacia frente a la marchitez vascular del tomate. Las conidias formuladas de PO212 se obtuvieron por la adición conjunta de distintos aditivos (mojantes, adherentes o estabilizantes) en dos momentos diferentes del proceso de producción/secado: i) antes del proceso de producción (en la bolsa de fermentación) en el momento de la inoculación de las bolsas de fermentación con conidias de PO212 o ii) antes del secado en el momento de la resuspensión de las conidias tras su centrifugación. De las 22 nuevas formulaciones desarrolladas y evaluadas en plantas de tomate en ensayos en invernadero, seis de ellas (FOR22, FOR25, FOR32, FOR35, FOR36 y FOR37) mejoran significativamente (P=0,05) el control de la marchitez vascular del tomate con respecto al obtenido con las conidias secas de P.oxalicum sin aditivos (CSPO) o con el fungicida Bavistin. Los formulados que mejoran la eficacia de las conidias secas sin aditivos son aquellos que contienen como humectantes alginato sódico en fermentación, seguido de aquellos que contienen glicerol como estabilizante en fermentación, y metil celulosa y leche desnatada como adherentes antes del secado. Además, el control de la marchitez vascular del tomate por parte de los formulados de P. oxalicum está relacionado con la fecha de inicio de la enfermedad. Otra forma de continuar mejorando la eficacia de biocontrol es mejorar la materia activa mediante la SELECCIÓN DE NUEVAS CEPAS de P. oxalicum, las cuales podrían tener diferentes niveles de eficacia. De entre las 28 nuevas cepas de P. oxalicum ensayadas en cámara de cultivo, sólo el aislado PO15 muestra el mismo nivel de eficacia que PO212 (62-67% de control) frente a la marchitez vascular del tomate en casos de alta presión de enfermedad. Mientras que, en casos de baja presión de enfermedad todas las cepas de P. oxalicum y sus mezclas demuestran ser eficaces. Finalmente, se estudia ampliar el rango de actuación de este ACB a OTROS HUÉSPEDES Y OTROS PATÓGENOS Y DIFERENTES GRADOS DE VIRULENCIA. En ensayos de eficacia de P. oxalicum frente a aislados de diferente agresividad de Verticillium spp. y Fusarium oxysporum f. sp. lycopersici en plantas de tomate en cámaras de cultivo, se demuestra que la eficacia de PO212 está negativamente correlacionada con el nivel de enfermedad causada por F. oxysporum f. sp. lycopersici pero que no hay ningún efecto diferencial en la reducción de la incidencia ni de la gravedad según la virulencia de los aislados. Sin embargo, en los ensayos realizados con V. dahliae, PO212 causa una mayor reducción de la enfermedad en las plantas inoculadas con aislados de virulencia media. La eficacia de PO212 también era mayor frente a aislados de virulencia media alta de F. oxysporum f. sp. melonis y F. oxysporum f. sp. niveum, en plantas de melón y sandía, respectivamente. En ambos huéspedes se demuestra que la dosis óptima de aplicación del ACB es de 107 conidias de PO212 g-1 de suelo de semillero, aplicada 7 días antes del trasplante. Además, entre 2 y 4 nuevas aplicaciones de PO212 a la raíces de las plantas mediante un riego al terreno de asiento mejoran la eficacia de biocontrol. La eficacia de PO212 no se limita a hongos patógenos vasculares como los citados anteriormente, sino también a otros patógenos como: Phytophthora cactorum, Globodera pallida y G. rostochiensis. PO212 reduce significativamente los síntomas (50%) causados por P. cactorum en plantas de vivero de fresa, tras la aplicación del ACB por inmersión de las raíces antes de su trasplante al suelo de viveros comerciales. Por otra parte, la exposición de los quistes de Globodera pallida y G. rostochiensis (nematodos del quiste de la patata) a las conidias de P. oxalicum, en ensayos in vitro o en microcosmos de suelo, reduce significativamente la capacidad de eclosión de los huevos. Para G. pallida esta reducción es mayor cuando se emplean exudados de raíz de patata del cv. 'Monalisa', que exudados de raíz del cv. 'Desirée'. No hay una reducción significativa en la tasa de eclosión con exudados de raíz de tomate del cv. 'San Pedro'. Para G. rostochiensis la reducción en la tasa de eclosión de los huevos se obtiene con exudados de la raíz de patata del cv. 'Desirée'. El tratamiento con P. oxalicum reduce también significativamente el número de quistes de G. pallida en macetas. Con el fin de optimizar la aplicación práctica de P. oxalicum cepa 212 como tratamiento biológico del suelo, es esencial entender cómo el entorno físico influye en la capacidad de colonización, crecimiento y supervivencia del mismo, así como el posible riesgo que puede suponer su aplicación sobre el resto de los microorganismos del ecosistema. Por ello en este segundo objetivo de esta tesis se estudia la interacción del ACB con el medio ambiente en el cual se aplica. Dentro de este objetivo se evalúa la INFLUENCIA DE LA TEMPERATURA, DISPONIBILIDAD DE AGUA Y PROPIEDADES FÍSICO-QUÍMICAS DE LOS SUELOS (POROSIDAD, TEXTURA, DENSIDAD...) SOBRE LA SUPERVIVENCIA Y EL CRECIMIENTO DE PO212 en condiciones controladas elaborando modelos que permitan predecir el impacto de cada factor ambiental en la supervivencia y crecimiento de P. oxalicum y conocer su capacidad para crecer y sobrevivir en diferentes ambientes. En las muestras de suelo se cuantifica: i) la supervivencia de Penicillium spp. usando el recuento del número de unidades formadoras de colonias en un medio de cultivo semi-selectivo y ii) el crecimiento (biomasa) de PO212 mediante PCR en tiempo real. En los resultados obtenidos se demuestra que P. oxalicum crece y sobrevive mejor en condiciones de sequía independientemente de la temperatura y del tipo de suelo. Si comparamos tipos de suelo P. oxalicum crece y sobrevive en mayor medida en suelos areno-arcillosos con un bajo contenido en materia orgánica, un mayor pH y una menor disponibilidad de fósforo y nitrógeno. La supervivencia y el crecimiento de P. oxalicum se correlaciona de forma negativa con la disponibilidad de agua y de forma positiva con el contenido de materia orgánica. Sólo la supervivencia se correlaciona también positivamente con el pH. Por otro lado se realizan ensayos en suelos de huertos comerciales con diferentes propiedades físico-químicas y diferentes condiciones ambientales para ESTUDIAR EL ESTABLECIMIENTO, SUPERVIVENCIA Y DISPERSIÓN VERTICAL Y MOVILIDAD HORIZONTAL DE PO212. P. oxalicum 212 puede persistir y sobrevivir en esos suelos al menos un año después de su liberación pero a niveles similares a los de otras especies de Penicillium indígenas presentes en los mismos suelos naturales. Además, P. oxalicum 212 muestra una dispersión vertical y movilidad horizontal muy limitada en los diferentes tipos de suelo evaluados. La introducción de P. oxalicum en un ambiente natural no sólo implica su actuación sobre el microorganismo diana, el patógeno, si no también sobre otros microorganismos indígenas. Para EVALUAR EL EFECTO DE LA APLICACIÓN DE P. oxalicum SOBRE LAS POBLACIONES FÚNGICAS INDIGENAS PRESENTES EN EL SUELO de dos huertos comerciales, se analizan mediante electroforesis en gradiente desnaturalizante de poliacrilamida (DGGE) muestras de dichos suelos a dos profundidades (5 y 10 cm) y a cuatro fechas desde la aplicación de P. oxalicum 212 (0, 75, 180 y 365 días). El análisis de la DGGE muestra que las diferencias entre las poblaciones fúngicas se deben significativamente a la fecha de muestreo y son independientes del tratamiento aplicado y de la profundidad a la que se tomen las muestras. Luego, la aplicación del ACB no afecta a la población fúngica de los dos suelos analizados. El análisis de las secuencias de la DGGE confirma los resultados anteriores y permiten identificar la presencia del ACB en los suelos. La presencia de P. oxalicum en el suelo se encuentra especialmente relacionada con factores ambientales como la humedad. Por tanto, podemos concluir que Penicillium oxalicum cepa 212 puede considerarse un óptimo Agente de Control Biológico (ACB), puesto que es ecológicamente competitivo, eficaz para combatir un amplio espectro de enfermedades y no supone un riesgo para el resto de microorganismos fúngicos no diana presentes en el lugar de aplicación. ABSTRACT Currently, reduction of active (EU) and the implementation of the new EU Directive 2009/128 which establishing the framework for action to achieve the sustainable use of chemical pesticides and preference of use of biological, physical and other non-chemical methods, forces to look for control methods less harmful to the environment. Biological control (CB) of plant diseases using biological control agents (BCA) is perceived as a safer alternative and with less environmental impact, either alone or as part of an integrated control strategy. The isolate 212 of Penicillium oxalicum (PO212) (ATCC 201888) was originally isolated from the soil mycoflora in Spain. P. oxalicum is a promising biological control agent for Fusarium wilt and other tomato diseases. Once identified and characterized the BCA, was developed a mass production method of conidia by solid-state fermentation. After determined the process of obtaining a formulated product of the BCA by drying of product by fluid-bed drying, it enables the preservation of the inoculum over a long period of time. Finally, some formulations of dried P. oxalicum conidia have been developed which contain one different additive that have improved their viability, stability and facilitated its handling and application. However, further work is needed to improve biocontrol efficacy. The first objective of this thesis has focused on the study of the interaction BCA- pathogen-host, to allow P.oxalicum to work in different pathosystems. The first point to be addressed in this objective is the development of new FORMULATIONS of BCA which increase their effectiveness against vascular wilt of tomato. PO212 conidial formulations were obtained by the joint addition of various additives (wetting agents, adhesives or stabilizers) at two different points of the production-drying process: i) to substrate in the fermentation bags before the production process, and (ii) to conidial paste obtained after production but before drying. Of the 22 new formulations developed and evaluated in tomato plants in greenhouse tests, six of them (FOR22 , FOR25 , FOR32 , FOR35 , FOR36 and FOR3) improved significantly (P = 0.05) the biocontrol efficacy against tomato wilt with respect to that obtained with dried P.oxalicum conidia without additives (CSPO) or the fungicide Bavistin. The formulations that improve the efficiency of dried conidia without additives are those containing as humectants sodium alginate in the fermentation bags, followed by those containing glycerol as a stabilizer in the fermentation bags, and methylcellulose and skimmed milk as adherents before drying. Moreover, control of vascular wilt of tomatoes by PO212 conidial formulations is related to the date of disease onset. Another way to further improve the effectiveness of biocontrol is to improve the active substance by SELECTION OF NEW STRAINS of P. oxalicum, which may have different levels of effectiveness. Of the 28 new strains of P. oxalicum tested in a culture chamber, only PO15 isolate shows the same effectiveness that PO212 (62-67 % of control) against tomato vascular wilt in cases of high disease pressure. Whereas in cases of low disease pressure all strains of P. oxalicum and its mixtures effective. Finally, we study extend the range of action of this BCA TO OTHER GUESTS AND OTHER PATHOGENS AND DIFFERENT DEGREES OF VIRULENCE. In efficacy trials of P. oxalicum against isolates of different aggressiveness of Verticillium spp. and Fusarium oxysporum f. sp. lycopersici in tomato plants in growth chambers, shows that the efficiency of PO212 is negatively correlated with the level of disease caused by F. oxysporum f. sp. lycopersici. There is not differential effect in reducing the incidence or severity depending on the virulence of isolates. However, PO212 cause a greater reduction of disease in plants inoculated with virulent isolates media of V. dahlia. PO212 efficacy was also higher against isolates of high and average virulence of F. oxysporum f. sp. melonis and F. oxysporum f. sp. niveum in melon and watermelon plants, respectively. In both hosts the optimum dose of the BCA application is 107 conidia PO212 g-1 soil, applied on seedlings 7 days before transplantation into the field. Moreover, the reapplication of PO212 (2-4 times) to the roots by irrigation into the field improve efficiency of biocontrol. The efficacy of PO212 is not limited to vascular pathogens as those mentioned above, but also other pathogens such as Oomycetes (Phytophthora cactorum) and nematodes (Globodera pallida and G. rostochiensis). PO212 significantly reduces symptoms (50 %) caused by P. cactorum in strawberry nursery plants after application of BCA by dipping the roots before transplanting to soil in commercial nurseries. Moreover, the exposure of G. pallida and G. rostochiensis cysts to the conidia of P. oxalicum, in in vitro assays or in soil microcosms significantly reduces hatchability of eggs. The reduction in the rate of G. pallida juveniles hatching was greatest when root diffusates from the `Monalisa´ potato cultivar were used, followed by root diffusates from the `Désirée´ potato cultivar. However, no significant reduction in the rate of G. pallida juveniles hatching was found when root diffusates from the ‘San Pedro” tomato cultivar were used. For G. rostochiensis reduction in the juveniles hatching is obtained from the root diffusates 'Desirée' potato cultivar. Treatment with P. oxalicum also significantly reduces the number of cysts of G. pallida in pots. In order to optimize the practical application of P. oxalicum strain 212 as a biological soil treatment, it is essential to understand how the physical environment influences the BCA colonization, survival and growth, and the possible risk that can cause its application on other microorganisms in the ecosystem of performance. Therefore, the second objective of this thesis is the interaction of the BCA with the environment in which it is applied. Within this objective is evaluated the INFLUENCE OF TEMPERATURE, WATER AVAILABILITY AND PHYSICAL-CHEMICAL PROPERTIES OF SOILS (POROSITY, TEXTURE, DENSITY...) ON SURVIVAL AND GROWTH OF PO212 under controlled conditions to develop models for predicting the environmental impact of each factor on survival and growth of P. oxalicum and to know their ability to grow and survive in different environments. Two parameters are evaluated in the soil samples: i) the survival of Penicillium spp. by counting the number of colony forming units in semi-selective medium and ii) growth (biomass) of PO212 by real-time PCR. P. oxalicum grows and survives better in drought conditions regardless of temperature and soil type. P. oxalicum grows and survives more in sandy loam soils with low organic matter content, higher pH and lower availability of phosphorus and nitrogen. Survival and growth of P. oxalicum negatively correlates with the availability of water and positively with the organic content. Only survival also correlated positively with pH. Moreover, trials are carried out into commercial orchards soils with different physic-chemical properties and different environmental conditions TO STUDY THE ESTABLISHMENT, SURVIVAL, VERTICAL DISPERSION AND HORIZONTAL SPREAD OF PO212. P. oxalicum 212 can persist and survive at very low levels in soil one year after its release. The size of the PO212 population after its release into the tested natural soils is similar to that of indigenous Penicillium spp. Furthermore, the vertical dispersion and horizontal spread of PO212 is limited in different soil types. The introduction of P. oxalicum in a natural environment not only involves their action on the target organism, the pathogen, but also on other indigenous microorganisms. TO ASSESS THE EFFECT OF P. oxalicum APPLICATION ON SOIL INDIGENOUS FUNGAL COMMUNITIES in two commercial orchards, soil samples are analyzed by Denaturing Gradient Gel Electrophoresis polyacrylamide (DGGE). Samples are taken from soil at two depths (5 and 10 cm) and four dates from the application of P. oxalicum 212 (0, 75, 180 and 365 days). DGGE analysis shows that differences are observed between sampling dates and are independent of the treatment of P. oxalicum applied and the depth. BCA application does not affect the fungal population of the two soil analyzed. Sequence analysis of the DGGE bands confirms previous findings and to identify the presence of BCA on soils. The presence of P. oxalicum in soil is especially related to environmental factors such as humidity. Therefore, we conclude that the 212 of strain Penicillium oxalicum can be considered an optimum BCA, since it is environmentally competitive and effective against a broad spectrum of diseases and does not have any negative effect on soil non-target fungi communities.

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Changes in fluidization behaviour of green peas particulates with change in moisture content during drying were investigated using a fluidized bed dryer. All drying experiments were conducted at 50 + 2 0C and 13 + 2 % RH using a heat pump dehumidifier system. Fluidization experiments were undertaken for the bedheights of 100, 80, 60 and 40 mm and at 10 moisture content levels. Fluidization behaviour was best fitted to the linear model of Umf = A + B m. A generalized model was also formulated using the height variation. Also generalized equation and Ergun equation was used to compare minimum fluidization velocity. Copyright ©2006 The Berkeley Electronic Press. All rights reserved.