913 resultados para Chlorine Industry, Electrochemical Processes, Photovoltaic, Sodium Chloride, Solar Energy


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This collective monography by a group of lithologists from the Geological Institute of the USSR Academy of Sciences summarizes materials of the Deep-Sea Drilling Project from the Atlantic Ocean. It gives results of processing materials on the sequences drilled during DSDP Legs 41, 45, 48 and 49. These studies were based on lithological-facial analysis combined with detailed mineralogical-petrographic description. Its chapters give a number of ideas on formation of the Earth sedimentary cover, which can be used for compilation of regional and global schemes of ocean paleogeography, reconstruction of history of some structures in the World Ocean, correlation between sedimentary processes on continents and in oceans, estimation of perspectives for oil and gas fields and ore formation.

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In Brazil, a low-latitude country characterized by its high availability and uniformity of solar radiation, the use of PV solar energy integrated in buildings is still incipient. However, at the moment there are several initiatives which give some hints that lead to think that there will be a change shortly. In countries where this technology is already a daily reality, such as Germany, Japan or Spain, the recommendations and basic criteria to avoid losses due to orientation and tilt are widespread. Extrapolating those measures used in high latitudes to all regions, without a previous deeper analysis, is standard practice. They do not always correspond to reality, what frequently leads to false assumptions and may become an obstacle in a country which is taking the first step in this area. In this paper, the solar potential yield for different surfaces in Brazilian cities (located at latitudes between 0° and 30°S) are analyzed with the aim of providing the necessary tools to evaluate the suitability of the buildings’ envelopes for photovoltaic use

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Dual-junction solar cells formed by a GaAsP or GaInP top cell and a silicon bottom cell seem to be attractive candidates to materialize the long sought-for integration of III?V materials on silicon for photovoltaic applications. When manufacturing a multi-junction solar cell on silicon, one of the first processes to be addressed is the development of the bottom subcell and, in particular, the formation of its emitter. In this study, we analyze, both experimentally and by simulations, the formation of the emitter as a result of phosphorus diffusion that takes place during the first stages of the epitaxial growth of the solar cell. Different conditions for the Metal-Organic Vapor Phase Epitaxy (MOVPE) process have been evaluated to understand the impact of each parameter, namely, temperature, phosphine partial pressure, time exposure and memory effects in the final diffusion profiles obtained. A model based on SSupremIV process simulator has been developed and validated against experimental profiles measured by ECV and SIMS to calculate P diffusion profiles in silicon formed in a MOVPE environment taking in consideration all these factors.

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Production of back contact solar cells requires holes generations on the wafers to keep both positive and negative contacts on the back side of the cell. This drilling process weakens the wafer mechanically due to the presence of the holes and the damage introduced during the process as microcracks. In this study, several chemical processes have been applied to drilled wafers in order to eliminate or reduce the damage generated during this fabrication step. The treatments analyzed are the followings: alkaline etching during 1, 3 and 5 minutes, acid etching for 2 and 4 minutes and texturisation. To determine mechanical strength of the samples a common mechanical study has been carried out testing the samples by the Ring on Ring bending test and obtaining the stress state in the moment of failure by FE simulation. Finally the results obtained for each treatment were fitted to a three parameter Weibull distribution

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Laser processing has been the tool of choice last years to develop improved concepts in contact formation for high efficiency crystalline silicon (c-Si) solar cells. New concepts based on standard laser fired contacts (LFC) or advanced laser doping (LD) techniques are optimal solutions for both the front and back contacts of a number of structures with growing interest in the c-Si PV industry. Nowadays, substantial efforts are underway to optimize these processes in order to be applied industrially in high efficiency concepts. However a critical issue in these devices is that, most of them, demand a very low thermal input during the fabrication sequence and a minimal damage of the structure during the laser irradiation process. Keeping these two objectives in mind, in this work we discuss the possibility of using laser-based processes to contact the rear side of silicon heterojunction (SHJ) solar cells in an approach fully compatible with the low temperature processing associated to these devices. First we discuss the possibility of using standard LFC techniques in the fabrication of SHJ cells on p-type substrates, studying in detail the effect of the laser wavelength on the contact quality. Secondly, we present an alternative strategy bearing in mind that a real challenge in the rear contact formation is to reduce the damage induced by the laser irradiation. This new approach is based on local laser doping techniques previously developed by our groups, to contact the rear side of p-type c-Si solar cells by means of laser processing before rear metallization of dielectric stacks containing Al2O3. In this work we demonstrate the possibility of using this new approach in SHJ cells with a distinct advantage over other standard LFC techniques.

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Tanto el tema de esta investigación, como sus objetivos, fundamentos, materiales seleccionados y parte experimental para alcanzarlos, han sido promovidos por la situación y el estado de las construcciones de hormigón armado que se comenzaron a realizar en España a partir del año 1975, con hormigones y morteros de cemento que contenían cenizas volantes hasta un 20 %, en principio, y hasta un 35 %, más tarde, de su dosificación de cemento Portland (CP), los cuales y en contra de lo esperado, han demandado y continúan demandando, muy a pesar de sus aparentes bondades de todo tipo que se les atribuían, una necesidad de mejora de sus prestaciones, especialmente, debido a un nivel inesperadamente bajo de la durabilidad de algunas obras construidas con los mismos. Todo era debido, en definitiva, a que las adiciones puzolánicas, naturales y artificiales, tales como las cenizas volantes, referidas antes, se vienen utilizando reglamentariamente para la fabricación de cementos y/o de sus productos derivados, hormigones, morteros y pastas, en la mayor parte de los países industrializados, desde hace ya más de tres décadas aproximadamente, en las mismas condiciones e idénticos usos constructivos que los hormigones y morteros de CP puro, viniendo además, dictada dicha utilización de estos materiales residuales, hoy sub-productos industriales, por cuestiones medioambientales y/o económicas, principalmente, motivo por el cual esta Tesis Doctoral ha pretendido responder también, adecuadamente y de manera esquemática (en forma de diagrama de flujo), a los criterios que deben de tenerse en cuenta a la hora de su selección y caracterización normalizada y reglamentada de estas adiciones minerales activas, sobre todo, antes de su dosificación y uso en forma del denominado cemento Portland con puzolana, o con ceniza volante, o con esquistos calcinados o con puzolanas calcinadas o con humo de sílice, cemento Portland mixto, cemento puzolánico o cemento compuesto, para que dichos problemas no se le produzcan al hormigón armado ni en masa. De aquí el enfoque tan particular y especial de esta investigación, al haberla circunscrito únicamente a las puzolanas naturales y artificiales, por considerarlas todas ellas, independientemente de por su origen, como materiales constituidos por pequeñas fracciones cristalinas distribuidas aleatoriamente en una matriz mayoritariamente vítrea y/o amorfa, la cual es la que le confiere su reactividad con el hidróxido de calcio en forma de cal apagada o de portlandita procedente de la hidratación del CP. A su vez, dichas fracciones vítreas y/o amorfas están constituidas, en su mayor parte, por sílice reactiva, SiO2r-, alúmina reactiva, Al2O3r-, y óxido de hierro reactivo, Fe2O3r-, recibiendo además, en conjunto, el nombre específico de "factores hidráulicos" de la puzolana, los cuales, por lo común, difieren cuantitativamente de sus contenidos totales, determinados por fusión alcalina mediante procedimientos normalizados. De los tres óxidos reactivos mencionados y desde el punto de vista técnico, los más importantes por su mayor presencia en casi todas las puzolanas naturales y artificiales y, también, transcendencia en la durabilidad química que les pueden llegar a conferir al hormigón armado y en masa, mortero o pasta de cemento que las contenga, son la SiO2r- y la Al2O3r-. El primero de los dos, la SiO2r-, reacciona nada más que con la portlandita (y el Ca(OH)2) para formar geles C-S-H, más tarde transformados en tobermoritas o en jennitas, semejantes a los que originan la alita y la belita del CP en su hidratación. Y desde el punto de vista normativo, la presencia de esta fracción silícica reactiva en las puzolanas viene regulada por la norma EN 197-1, de modo general, siendo además referida por la norma EN 450-1:2006, en el contexto de las cenizas volantes en su adición al hormigón, como "un polvo fino de partículas principalmente de forma esférica y cristalina, procedentes de la combustión de carbón pulverizado, que tiene propiedades puzolánicas y que está compuesto fundamentalmente de SiO2 y Al2O3". Además y de acuerdo con la primera de las dos normas, "El contenido de dióxido de silicio reactivo (definido y determinado según la norma EN 196-2 o su equivalente la UNE 80225) no debe ser inferior al 25 % en masa". Por su parte, cuantiosos estudios experimentales realizados por Talero solo y con otros investigadores, han demostrado que si la puzolana no es adecuada en calidad ni en cantidad, la durabilidad del cemento del que forme parte, y, por consiguiente, de los productos derivados que con él se fabriquen, hormigones, morteros, pastas y prefabricados, puede llegar a ser anormalmente baja, porque la alúmina reactiva, Al2O3r-, o alúmina tetra- o penta-coordinada que la constituye, se implica como tal, de una forma muy directa y con resultados totalmente contrapuestos incluso, en los ataques químicos agresivos naturales que se les producen, provenientes de terrenos y aguas selenitosas (sulfatos, que atacan en su caso al propio material hormigón, mortero y pasta que la contiene para formar ettringita de rápida formación, ett-rf, la cual puede llegar incluso a provocar un ataque rápido del yeso), del rocío marino y de las sales de deshielo (cloruros, que atacan, en cambio, a las armaduras de acero del hormigón provocándoles su corrosión electroquímica por "picadura", si bien, en este otro ataque químico, dicha Al2O3r- lo que origina es sal de Friedel de rápida formación, sF-rf, también, cuyo efecto es, en cambio, colmatador y protector, en definitiva, de dicha corrosión electroquímica), del agua de mar (acción agresiva mutua de cloruros y sulfatos), de la carbonatación, de la reactividad árido-álcali, además de intervenir en la liberación del calor de hidratación, así como también, en el comportamiento reológico de sus pastas, etc., acortándoles de este modo su durabilidad prevista y, en ocasiones, muy seriamente incluso. Pero lo más paradójico de todo es, que a pesar de su referido comportamiento totalmente contrapuesto, frente a sulfatos y cloruros, - aún no se dispone de un método de análisis químico para su determinación cuantitativa, que sea además relativamente sencillo en su operatividad, veraz, preciso, de respuesta rápida, desde el punto de vista técnico de la construcción (no más de 28 días), repetible, reproducible, que no implique peligro alguno para la seguridad vital de las personas que lo tengan que manipular y poner en práctica, económico, y que sirva también tanto para investigación -vertiente científica-, como, sobre todo, para control de calidad -vertiente técnica-, - y ni mucho menos tampoco se dispone todavía, de especificación química alguna que precise el contenido máximo de Al2O3r- (%) que tiene que poseer una puzolana natural o artificial, para poder ser añadida al cemento Portland y/o al hormigón que va a estar sometido a un determinado ataque químico agresivo de los mencionados antes, y, en especial, a sulfatos, a cloruros o al agua de mar. Y para mayor justificación de ambas necesidades, se ha de decir también que la vigente Instrucción de Hormigón Estructural EHE-08 no contempla tampoco especificación química alguna sobre los "factores hidráulicos", en general, ni del contenido de Al2O3r-(%) de las cenizas volantes, muy en particular, en su Artículo 30º "Adiciones", ni en ningún otro Artículo, a pesar de que sí contempla, en cambio, - otras especificaciones químicas que carecen del necesario significado en cuanto a la necesidad de llevar explícita o implícitamente, el mensaje de la Durabilidad Química deseado, y - el Artículo 37º, el cual y para mayor abundamiento se titula paradójicamente "Durabilidad del hormigón y de las armaduras". Asimismo, tampoco se contempla en la última versión que acaba de publicarse de la norma EN 197-1 titulada: "Cementos. Parte 1: Composición, especificaciones y criterios de conformidad de los cementos comunes". Ni tampoco, en la norma EN 450-1:2006 titulada "Cenizas volantes para hormigón. Parte 1: Definiciones, especificaciones y criterios de conformidad", ni en la vigente Instrucción española para la Recepción de Cementos, RC-08, ni en la norma ASTM C618-03 tampoco. La única especificación química que ambas normas, la europea y la norteamericana, refieren es aquella que dice que la suma de los contenidos porcentuales de SiO2 total, Al2O3 total y Fe2O3 total, de la puzolana natural o artificial, ha de ser mayor o igual que 70 %, definiendo, además, a las puzolanas de este modo tan genérico: "materiales silíceos o silíceos y aluminosos, que por sí mismos no poseen valor cementante alguno, pero que finamente divididos y en presencia de humedad, reaccionarán químicamente con hidróxido de calcio a temperaturas ordinarias para formar compuestos que poseen propiedades cementantes". Por consiguiente y de acuerdo con todo lo anterior, el objetivo primordial de esta Tesis Doctoral ha sido: Diseñar y poner a punto un nuevo método analítico de utilidad técnica (que la duración máxima del ensayo no sea mayor de 28 días), para determinar el contenido de alúmina reactiva, vítrea o amorfa, Al2O3r-, de las puzolanas naturales y artificiales. Y una vez puesto a punto, validarlo a nivel de su repetibilidad, de acuerdo con parámetros estadísticos apropiados, poniendo especial énfasis en los criterios de aceptación establecidos por la American Association of Official Analytical Chemists (AOAC). Y para conseguirlo, la innovación de esta investigación se ha basado en los siguientes fundamentos generales, a saber: - Toda la alúmina de cualquier puzolana natural o artificial, capaz de ser atacada, disuelta y lixiviada en 28 días, por la portlandita o por el hidróxido de calcio, Ca(OH)2, en medio acuoso, es considerada como alúmina reactiva, Al2O3r-. - Dicha fracción alumínica reactiva de la puzolana natural o artificial se tiene que encontrar, además, en el estado físico-químico de poder reaccionar químicamente también, en presencia de hidróxido de calcio, cloruro de sodio y agua, para originar monocloro¿aluminato de calcio hidratado, C3A·CaCl2·10H2O, o sal de Friedel. Además, dicho estado físico-químico de la puzolana ha de ser acorde con la definición de alúmina reactiva adoptada en esta investigación en razón de las prestaciones reales de durabilidad química que le puede llegar a conferir a los cementos de mezcla y a sus productos derivados, hormigones, morteros y pastas, que se fabriquen con la misma. - La originalidad de este nuevo método analítico, respecto a los demás métodos ya existentes, reside en que la cuantificación de dicha fracción alumínica reactiva de la puzolana natural o artificial, se realiza mediante cálculo estequiométrico, basándose, para ello, en dicha reacción química de formación de sal de Friedel precisamente, tras 28 días de hidratación básica-salina acelerada de la puzolana natural o artificial, habiéndose realizado, además, en esta investigación dicha determinación cuantitativa de la cantidad de sal de Friedel originada por cada puzolana, mediante dos técnicas analíticas instrumentales que fueron las siguientes: el análisis termogravimétrico (variante I ó I-I en su caso) y el método de Rietveld con la difracción de Rayos X en polvo (variante II). - La reacción química de formación de sal de Friedel tras 28 días de hidratación básica-salina acelerada de las puzolanas que se analicen, se optimizó para asegurar que el único compuesto químico de aluminio y cloro formado fuese sal de Friedel nada más (dosificando para ello en cantidad adecuada los reactivos químicos necesarios: Ca(OH)2, NaCl y agua destilada), manteniendo, además y por otra parte, el compromiso apropiado entre el máximo rendimiento de dicha reacción química (ataque, disolución y lixiviación en 28 días, de toda la alúmina reactiva de la puzolana) y el modo y medios más adecuados de acelerarlo para conseguirlo fue a 40°C de temperatura, con agitación constante y cierre hermético del reactor. - La aplicabilidad y selectividad del nuevo método analítico, objeto de esta Tesis Doctoral, fue estudiada con una serie de puzolanas naturales y artificiales españolas, silíceas y/o silíceas y aluminosas en naturaleza, que fueron las siguientes: M0 (metacaolín 0), M1 (M0 con 50 % de cuarzo), C y L (puzolanas naturales de las Islas Canarias), CV10 y CV17 (cenizas volantes), A (puzolana natural de Almagro), O (puzolana natural de Olot) y HS (humo de sílice). - Todas las adiciones minerales anteriores cumplieron con los principales requisitos físicos y químicos que son preceptivos para poder considerarlas, antes de todo, como puzolanas, lo que era indispensable y de obligado cumplimiento, para poderles determinar su contenido total de Al2O3r- (%) mediante el nuevo método analítico. Estos condicionantes fueron los siguientes: grado adecuado de finura de molido o tamaño medio de partícula (según la norma EN 451-2), haber sido analizadas químicamente antes de todo (según la norma EN 196-2 ó la ASTM C311), con el fin de determinarles especialmente, sus contenidos totales de SiO2 (%), Al2O3 (%) y Fe2O3 (%), haberles determinado, además, su contenido de sílice reactiva, SiO2r- (%) (según la norma UNE 80225), y haber cumplido con el ensayo de puzolanicidad o de Frattini (según la norma EN 196-5) a la edad de 28 días al menos. Este último requisito, otrora de obligado cumplimiento hasta el año 1988, para cualquier puzolana natural y artificial que una fábrica de cementos pretendiera introducir en el proceso de fabricación de un nuevo cemento puzolánico o cemento tipo CEM IV, ha logrado así, que se tenga que volver utilizar de nuevo de forma obligada con esta Tesis Doctoral. Y los resultados obtenidos con el nuevo método analítico de los contenidos de Al2O3r-(%) de las puzolanas seleccionadas, fueron los siguientes: - Mediante su variante I: M0 29.9 %, M1 16.9 %, CV10 11.4 %, L 12.3 %, C 12.6 %, A 8.0 %, CV17 9.5 % y O 6.3 % de Al2O3r-, y - Mediante su variante II: M0 30.7 %, M1 15.4 %, CV10 14.7%, L 11.8 %, C 11.1 %, A 8.9 %, CV17 9.6 % y O 6.8 % de Al2O3r-. Finalmente, todos ellos fueron contrastados, además, mediante la calibración y validación del nuevo método analítico, con los valores de referencia obtenidos de esas mismas puzolanas, los cuales se les habían determinado mediante el método de Florentín, consistente en atacar, disolver y lixiviar también toda la fracción alumínica soluble de la puzolana (y además, aquella silícica y férrica que la constituyen a la par), pero, en especial, su contenido total de alúmina reactiva, mediante un ataque básico (con Ca(OH)2 en medio acuoso a temperatura del laboratorio, habiendo sido, además, su duración hasta 1 año), seguido de otro ácido (con HCl, d = 1.12), habiéndose obtenido esta vez los siguientes resultados de sus contenidos de Al2O3r- (%): M0 28.8 %, M1 16.7 %, CV10 9.7 %, L 11.2 %, C 12.2 %, A 13.0 %, CV17 10.6 % y O 9.5 %. Dicha validación realizada ha puesto de manifiesto, en términos generales, que el nuevo método analítico es más fidedigno que el de Florentín, por lo que resulta ser totalmente apropiado para obtener los resultados que se han pretendido, además de proporcionarlos en un espacio de tiempo relativamente corto (28 días a lo sumo) y a un coste económico razonable por no elevado (salvo error u omisión y libre de impuestos directos e indirectos, el coste económico estimado de la variante I estaría en torno a 800.00 - 900.00 €/puzolana -caso más probable-, y aproximadamente una tercera parte nada más, en el caso de que la edad máxima del ensayo acelerado sea 7 días nada más -caso menos probable-), y, por consiguiente, técnicamente aceptable, al cumplir, además, en todo el rango considerado de variabilidad posible de concentraciones o contenidos del analito buscado en la puzolana, con tales parámetros de validación como son: linealidad (los resultados obtenidos son directamente proporcionales a la señal-respuesta instrumental recibida), sensibilidad, precisión excelente, repetibilidad satisfactoria de los valores obtenidos de los contenidos de Al2O3r- de todas y cada una de las adiciones puzolánicas seleccionadas, confirmando, por ello, la universalidad de su uso. Finalmente, las ventajas del nuevo método analítico, respecto a los métodos ya existentes recopilados de la bibliografía (el método de Florentín, el método de López Ruiz -HF 40 % y HNO3 2N-, el método de Murat y Driouche para arcillas -HF 0.5M-, el método de Arjuan, Silbee y Roy para cenizas volantes -HF 1 %- y su modificación por Fernández-Jiménez y cols. -HF 1 %, 27Al NMR MAS y XRD (método de Rietveld)-, y el método de determinación de la relación SiO2r-/Al2O3r- para arcillas y cenizas volantes por Ruiz-Santaquiteria y cols. -HF 1 %, NaOH 8M y ICP-AES-) son, principalmente, estar exento de peligro alguno para la seguridad vital de las personas que lo tengan que manipular y poner en práctica, ser bastante apropiado para control de calidad además de para investigación, su considerable menor coste económico, su relativamente corto espacio de tiempo que se necesita para obtener la respuesta-resultado pretendida (28 días a lo sumo), así como su universalidad y selectividad, puesto que además, su aplicabilidad es para todo tipo de adiciones puzolánicas naturales o artificiales, como así lo demuestran los resultados obtenidos de los materiales puzolánicos naturales y artificiales seleccionados y analizados, en un rango de concentraciones del analito -contenido de alúmina reactiva, Al2O3r- (%)-, desde el 5 % hasta el 30 % en masa, rango éste que, por otra parte, comprende prácticamente TODAS las adiciones puzolanas naturales y artificiales existentes en el mercado transnacional y las aún por existir. Por consiguiente y de acuerdo con lo anterior, el nuevo método analítico, ya sea realizado mediante su variante I o la II, debido, - en primer lugar, a los fundamentados planteamientos relativos a su procedimiento experimental -modus operandi- el cual ha sido aplicado a una amplia gama de puzolanas naturales y artificiales, y - en segundo lugar, debido a la calidad de los resultados obtenidos con un grado de precisión y repetibilidad excelentes, ha demostrado poseer una gran utilidad científica -para investigación-, pero, sobre todo, técnica -para control de calidad de adiciones puzolánicas naturales y artificiales que se adicionan habitualmente al cemento Portland en fábrica y/o a sus hormigones y morteros en planta-, además de ser representativos los valores obtenidos mediante el mismo respecto a la más que probable durabilidad química que cada una de ellas puede llegarle a conferir al hormigón armado y en masa, mortero y pasta del que forme parte, así como también su cantidad adecuada de sustitución parcial de cada cemento Portland para conseguirla, acorde con sus propias prestaciones químico-físicas o físico-químicas que puede llegarle a conferir, según sea su carácter químico (alumínico, alumínico-silícico, silícico-alumínico, silícico-férrico-alumínico o silícico), forma y tamaño medio de su partícula. Por último, el nuevo método analítico ha demostrado cumplir además, con todos los requisitos de obligado cumplimiento que establece la norma ISO/IEC 17025 sobre la calidad y fiabilidad de nuevos métodos o procedimientos analíticos no normalizados todavía, para poder ser propuesto en un futuro próximo, ante la Comisión de AENOR correspondiente, con objeto de comenzar un expediente para su certificación y normalización. ________________________________________________________________________________ Both the subject of this research, its objectives, fundamentals, materials selected and experimental part to achieve, have all been promoted by the situation and the state of reinforced concrete constructions that began performing in Spain from 1975, with concrete and mortars cement containing fly ash up to 20 %, in principle, and later, up to 35 % to its content of Portland cement, which and against expected, demanded a need to improve their performance, especially due to an unexpectedly low level of durability of some works built with them, despite, however, its apparent benefits of all kinds are ascribed to them. Ultimately, the natural or artificial pozzolanic additions, such as fly ash specially, referred to above, have been used with regulation to manufacture cements and/or its derivatives, concretes, mortars, cement pastes, in the most industrialized countries. More than three decades ago, under the same conditions and identical construction mainly uses concretes and mortars plain Portland cement, besides coming, given that use of these waste materials, industrial by-products today for environmental and/or economic issues. For this reason, this Doctoral Thesis aims to answer properly and schematically (in the form of flow chart), the criteria to be taken into account when selection and characterization standardized for these active mineral additions, especially prior to choosing and use in the so-called Portland Cement (PC) pozzolan, or with fly ash or with calcined shales or with calcined pozzolans or with silica fume or PC mixed or pozzolanic cement or compound cement, for that such pathology problems will not occur when reinforced concretes nor mass concretes are used for building. Hence the very particular and special focus about this research, having confined only to the natural or artificial pozzolans, considering them all, regardless of their origin, approach as materials consisting of small crystalline fractions randomly distributed in a largely vitreous and/or amorphous matrix, which confers their reactivity with calcium hydroxide in the form of slaked lime or portlandite from PC. In turn, these vitreous and/or amorphous fractions consist in its greater part, by reactive silica, SiO2r-, reactive alumina, Al2O3r-, and reactive iron oxide, Fe2O3r-, which also receive, in conjunction, the specific name of "hydraulic factors" of the pozzolan. Usually, they all differs in quantity of their respective total contents of the SiO2 (%), Al2O3 (%) and Fe2O3 (%) determined the pozzolan by alkaline fusion by means of standard procedures. Of the three above-mentioned oxides reagents and from the technical point of view, the most important for its increased presence in every one of the natural or artificial pozzolans and also significance in the chemical durability that can get them to give the concrete mortar or cement paste which contain them, are SiO2r- and Al2O3r-. From the first two, the SiO2r- reacts with portlandite only, released in the hydration of the PC (and with Ca(OH)2), to form C-S-H gels, transformed in tobermorites or jennites later on, similar to C-S-H gels also originating from the alite and belite hydration in the CP. From the standardization criteria point of view, the presence of this silicic fraction in pozzolans is regulated at first, by the European standard EN 197-1, in general, also being referred by the EN 450-1:2006, in the context of the fly ash in addition to the concrete, as a "fine powder of spherical particles mainly crystalline form. It is from the combustion of pulverized coal, which have pozzolanic properties and is mainly composed of SiO2 and Al2O3". In addition and according to the EN 197-1 standard, the reactive silica content (which can be defined and determined in accordance with EN 197-1 standard or its UNE 80225 standard) must not be lower than 25 % of its mass. Meanwhile, considerable experimental studies by Talero and Talero et al, have shown that if the pozzolan is not adequate in quality nor quantity, the durability of cement that is part and, therefore, of its derivative products, concretes, mortars and pastes cement, can become abnormally low because its reactive alumina, Al2O3r- (%), content or tetra- or penta-coordinated alumina which involves itself in a very direct and totally mixed and conflicting results even at all aggressive chemical attack natural to produce to the concrete, mortar and paste with inadequate natural and/or artificial pozzolans, such as those from the selenitous land and waters (sulfates, strikes if the material itself concrete, mortar and paste that contain them, for rapid forming ettringite form, ett-rf, which can even cause rapid gypsum attack to said concrete). In contrast, sea spray and de-icing salts (chlorides strikes the reinforced steel concrete causing them electrochemical corrosion by "bite", although in that other chemical attack, such Al2O3r- causes rapid Friedel's salt formation, Fs-rf, too, to cause protector effect of the electrochemical corrosion of reinforcements for these chlorides), seawater (mutual aggressive action of chlorides and sulfates), carbonation, alkali-silica reaction, and, in addition, to influence the release of hydration heat, as well as in the rheological behavior of the pastes, etc., decreasing/shorting them thus their expected durability and sometimes even very seriously. But the most ironic thing is, that despite its referral totally opposed, compared to sulfates and chlorides, behaviour, - far not available is, a chemical analysis method for its quantitative determination, which is also relatively simple in operation, accurate, precise, rapid response, from a technical point of view for building (no more than 28 days), repeatable, reproducible, not involving danger to life safety of the people who need to manipulate and implement, economic, and also serve for both scientific research and technical side, and - has yet to be any chemical specification that sets maximum levels for Al2O3r-(%) in the natural or artificial pozzolan to be added to the cement and/or to the concrete that will be subject to a particularly aggressive chemical attack from those mentioned above, and in particular, to sulphates, chlorides or sea water. And for the sake of and justification of this need, it has to be said that the current Spanish Instruction for Structural Concrete EHE-08 does not provide any specification on "hydraulic factors" in general, nor the content of Al2O3r- (%) in fly ash, very particular, as Article 30º "Additions", or any other Article, although does provide, however, other chemical specifications lacking the necessary meaning in terms of the message Chemical Durability mentioned, nor the Article 37º which and for greater sake, is paradoxically entitled "Durability of the concrete and of their reinforcements". It has also not contemplated in the latest version just released from EN 197-1 standard entitled "Cement Part 1: Composition, specifications and conformity criteria for common cements". Nor, in EN 450-1:2006 entitled "Fly ash for concrete Part 1: Definitions, specifications and conformity criteria", nor by current Spanish Instruction for Cement Reception, RC-08, nor the ASTM C618-03 Standard either. The only chemical specification that both Standards, European and American, refer is one that says that the sum of the total contents of SiO2 (%), Al2O3 (%) and Fe2O3 (%) of natural and artificial pozzolan, must be greater than or equal to 70 % , defining pozzolans thus: "siliceous or aluminous and siliceous materials, which themselves do not have any cementitious value but finely divided and in the presence of moisture it reacts with calcium hydroxide at ordinary temperatures to form compounds possessing cementitious properties". Consequently and according to everything related before, the primary objective of this Doctoral Thesis has been: To design and start-up a new quantitative analytical method of technical utility (the maximum test duration is not more than 28 days), to determine the content of reactive alumina content, Al2O3r- (%), vitreous or amorphous alumina, of natural and artificial pozzolans. And once designed, validate at repeatability level and in accordance with appropriate statistical parameters with special emphasis on the acceptance criteria established by the American Association of Official Analytical Chemists (AOAC). And to achieve this, the innovation of this research has been based on the following general principles, namely: - All the alumina in any pozzolan, natural or artificial, that can be attacked, dissolved and leached by portlandite or calcium hydroxide, Ca(OH)2, in aqueous medium, is considered reactive alumina, Al2O3r-. - This aluminic fraction of natural or artificial pozzolan to analyze and study, has to be in such physical-chemical state that it can react in the presence of calcium hydroxide, sodium chloride and water status and to cause monochloro-aluminate hydrated calcium, C3A·CaCl2·10H2O or Friedel's salt. Moreover, such physical-chemical state of the pozzolan must be consistent with the definition of reactive alumina adopted in this research because of the actual performance of chemical durability that can reach confer on blended cements and their derivatives, concretes, mortars and pastes that are manufactured with the same. - The originality of this new analytical method, compared to the other methods for determining reactive alumina existing (collected in abbreviated form in the state of the art of this report), is the quantification of such aluminic fraction of natural or artificial pozzolans is performed by stoichiometric calculation based on this, in the chemical reaction of Friedel's salt formation after 28 days of the analysis of saline-basic hydration accelerated natural or artificial pozzolan also performed in this research, and the quantitative determination of the Friedel's salt has been performed by two instrumental analytical techniques known as thermogravimetric analysis (variant I), and Rietveld method with X-ray powder diffraction (variant II). - The chemical reaction of Friedel's salt formation after 28 days of accelerated saline-basic hydration of the selected natural and artificial pozzolan, was optimized to ensure that the single chemical compound of aluminium and chlorine formed was Friedel's salt only (dosing for this purpose in amount suitable chemical reagents: Ca(OH)2, NaCl and distilled water), and, on the other hand, maintaining the appropriate compromise between the highest yield from the chemical reaction (attack, dissolution and leaching in 28 days, all reactive alumina of pozzolan) and to accelerate the etching media, which were 40°C temperature, constant stirring and sealing the reactor. - The applicability and selectivity of the new analytical method, the subject of this Doctoral Thesis, was studied with a series of Spanish natural and artificial pozzolans, siliceous or siliceous and aluminous in nature, which were as follows: M0 (metakaolin 0), M1 (M0 with 50 % quartz), L and C (natural pozzolans of the Canary Islands), CV10 (fly ash 10), CV17 (fly ash 17), A (natural pozzolan of Almagro), O (natural pozzolan of Olot), and HS (silica fume). - All mineral admixtures were selected satisfied the physical and chemical requirements proposed to consider them as pozzolan, which was mandatory, so its Al2O3r- (%) content can determine by the new analytical method. These conditions were as follows: adequate degree of fineness of grind or average particle size (according to EN 451-2 standard), have been analyzed chemically (according to EN 196-2 or ASTM C311 standards), in order to determine their total contents of SiO2 (%), Al2O3 (%) and Fe2O3 (%), mainly, having also determined its reactive silica content, SiO2r- (%) (UNE 80225 standard), and fulfilled with testing of pozzolanicity or Frattini test (according to EN 196-5 standard) at 28 days age at least. The last criteria was mandatory until 1988, for any natural and artificial pozzolan to a factory intended to introduce cements in the manufacturing process of a new Portland cement type CEM IV pozzolanic additions, and with this Doctoral Thesis has made is to be used once again mandatory. And the results obtained using the new analytical method, of the Al2O3r- (%) content for each selected pozzolan, were as follows: - by its variant I: M0 29.9 % , M1 16.9 % , CV10 11.4 % , L 12.3 % , C 12.6 % , A 8.0 % , CV17 9.5 % and O 6.3 % of Al2O3r-, and - by its variant II: M0 30.7 % , M1 15.4 % , CV10 14.7% % , L 11.8 % , C 11.1 % , A 8.9 % , CV17 9.6 % and O 6.8 % of Al2O3r-. Finally, they would all be further contrasted by the calibration and validation of new analytical method, with reference values obtained from these same natural and artificial pozzolans, which had been given by the method of Florentin, consisting of attack, dissolve and leached with a basic attack (with Ca(OH)2 in aqueous medium and laboratory temperature, having also been its duration up to 1 year), followed by another acid attack (HCl, d = 1.12), all soluble aluminic fraction of pozzolan, and in particular their total content of reactive alumina, Al2O3r-(%), was this time as follows: M0 28.8 %, M1 16.7 %, CV10 9.7 %, L 11.2 %, C 12.2 %, A 13.0 %, CV17 10.6 % and O 9.5 % (and their siliceous and iron contents that are at par). This validation has shown on the new analytical method is more reliable than Florentin method, so it turns out to be entirely appropriate to get the results that have been tried by the same, besides providing them a relatively short space of time (28 days at most) and reasonably no high economic cost (unless mistake -free direct and indirect taxes, such economic cost would be between 800.00 - 900.00 €/pozzolan (most likely case), and about an one-third part around, in the event that the maximum age of the accelerated test is 7 days only (less likely case). So it is technically acceptable, to consider the range of possible variability of concentrations or contents pozzolan analyte with validation parameters such as: linearity (the results obtained are directly proportional to the instrumental response signal received), excellent sensitivity and accuracy, satisfactory repeatability values from the contents of each and Al2O3r- (%) each selected pozzolan, confirming therefore universal use. Finally, the advantages of the new analytical method over existing methods compiled from literature (Florentin method , the Lopez Ruiz method -HF and HNO3 40 % 2N-, the method of Murat and Driouche for clays -0.5M HF-, the method of Arjuan, Roy and Silbee for fly ash -HF 1 %- and its modification by Fernández-Jiménez et al -HF 1 %, 27Al MAS NMR and XRD (Rietveld method)-, and the method for determining the SiO2r-/Al2O3r- clay and fly ash ratio of Santaquiteria Ruiz et al -HF 1 %, NaOH 8M and ICP-AES-) are primarily and relatively short time get the result intended answer (28 days at most), its considerable lower cost, free from danger to the life safety of the people who need to manipulate and put in practice as well as its universality and selectivity, since it is applicable for all types of natural or artificial pozzolans, as it has been shown by the results of selected natural and artificial pozzolanic materials and analyzed in a range of analyte concentrations -reactive alumina, Al2O3r- (%) content- from 5 % to 30 % by mass, this range, on the other hand, includes virtually ALL existing transnational market in natural and artificial pozzolans and still exist. Therefore and in accordance with the above, the new analytical method is already performed by the variant I or II, because, - firstly, grounded to experimental approaches concerning its experimental procedure -"modus operandi"- which has been applied to a wide range of natural and artificial pozzolans, and - secondly, due to the quality of the results obtained with a great degree of accuracy and repeatability, it has been shown to possess significant scientific value in the research, but especially technical value -for quality control of natural and artificial pozzolans commonly added to Portland cement factory and/or directly to their concrete and mortar in plant-, and also be representative enough of the values obtained by the same probable chemical durability that each of them can reach out to give the concrete mortar and paste to which it belongs, as well as proper amount of partial replacement of Portland cement. To get in line with their own chemical-physical or physical-chemical features which can come to confer, as its chemical character (aluminic, silicic-aluminic, aluminic-silicic, aluminic-ferric-silicic or ferric-silicic), form and medium size of its particle is. Finally, the new analytical method has proven to meet all mandatory requirements established by ISO/IEC 17025 on the quality and reliability of new methods or analytical procedures are not standardized yet, in order to be considered appropriate this new analytical method, in this Doctoral Thesis it is to be proposed in the near future, before the corresponding AENOR (Spanish Association for Standardization and Certification) Commission, to start a procedure for certification and standardization.

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The objective of this study was to propose a multi-criteria optimization and decision-making technique to solve food engineering problems. This technique was demostrated using experimental data obtained on osmotic dehydratation of carrot cubes in a sodium chloride solution. The Aggregating Functions Approach, the Adaptive Random Search Algorithm, and the Penalty Functions Approach were used in this study to compute the initial set of non-dominated or Pareto-optimal solutions. Multiple non-linear regression analysis was performed on a set of experimental data in order to obtain particular multi-objective functions (responses), namely water loss, solute gain, rehydration ratio, three different colour criteria of rehydrated product, and sensory evaluation (organoleptic quality). Two multi-criteria decision-making approaches, the Analytic Hierarchy Process (AHP) and the Tabular Method (TM), were used simultaneously to choose the best alternative among the set of non-dominated solutions. The multi-criteria optimization and decision-making technique proposed in this study can facilitate the assessment of criteria weights, giving rise to a fairer, more consistent, and adequate final compromised solution or food process. This technique can be useful to food scientists in research and education, as well as to engineers involved in the improvement of a variety of food engineering processes.

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Shading reduces the power output of a photovoltaic (PV) system. The design engineering of PV systems requires modeling and evaluating shading losses. Some PV systems are affected by complex shading scenes whose resulting PV energy losses are very difficult to evaluate with current modeling tools. Several specialized PV design and simulation software include the possibility to evaluate shading losses. They generally possess a Graphical User Interface (GUI) through which the user can draw a 3D shading scene, and then evaluate its corresponding PV energy losses. The complexity of the objects that these tools can handle is relatively limited. We have created a software solution, 3DPV, which allows evaluating the energy losses induced by complex 3D scenes on PV generators. The 3D objects can be imported from specialized 3D modeling software or from a 3D object library. The shadows cast by this 3D scene on the PV generator are then directly evaluated from the Graphics Processing Unit (GPU). Thanks to the recent development of GPUs for the video game industry, the shadows can be evaluated with a very high spatial resolution that reaches well beyond the PV cell level, in very short calculation times. A PV simulation model then translates the geometrical shading into PV energy output losses. 3DPV has been implemented using WebGL, which allows it to run directly from a Web browser, without requiring any local installation from the user. This also allows taken full benefits from the information already available from Internet, such as the 3D object libraries. This contribution describes, step by step, the method that allows 3DPV to evaluate the PV energy losses caused by complex shading. We then illustrate the results of this methodology to several application cases that are encountered in the world of PV systems design. Keywords: 3D, modeling, simulation, GPU, shading, losses, shadow mapping, solar, photovoltaic, PV, WebGL

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Esta tesis pretende contribuir al fomento y utilización de la energía solar como alternativa para la producción de agua caliente en el sector agroindustrial. La demanda de agua caliente es un aspecto clave en un gran número de agroindustrias y explotaciones agrarias. Esta demanda presenta una gran variabilidad, tanto en los horarios en que se solicita como en la temperatura del agua del depósito requerida (TADr), difiriendo del perfil de demanda habitual para uso doméstico. Existe una necesidad de profundizar en la influencia que tiene la variación de la TADr en la eficiencia y viabilidad de estos sistemas. El objetivo principal de esta tesis es caracterizar el funcionamiento de un sistema solar térmico (SST) con captador de tubos de vacío (CTV) para producir agua a temperaturas superiores a las habituales en estos sistemas. Se pretende determinar la influencia que la TADr tiene sobre la eficiencia energética del sistema, cuantificar el volumen de agua caliente que es capaz de suministrar en función de la TADr y determinar la rentabilidad del SST como sistema complementario de suministro. Para ello, se ha diseñado, instalado y puesto a punto un sistema experimental de calentamiento de agua, monitorizando su funcionamiento a diferentes TADr bajo condiciones ambientales reales. Los resultados cuantifican cómo el aumento de la TADr provoca una disminución de la energía suministrada al depósito, pudiendo superar diferencias de 1000 Wh m-2 d-1 entre 40 ºC y 80 ºC, para valores de irradiación solar próximos a 8000 Wh m-2 d-1 (la eficiencia del sistema oscila entre 73% y 56%). Esta reducción es consecuencia de la disminución de la eficiencia del captador y del aumento de las pérdidas de calor en las tuberías del circuito. En cuanto al agua suministrada, cuanto mayor es la TADr, mayor es la irradiación solar requerida para que tenga lugar la primera descarga de agua, aumentando el tiempo entre descargas y disminuyendo el número de éstas a lo largo del día. A medida que se incrementa la TADr, se produce una reducción del volumen de agua suministrado a la TADr, por factores como la pérdida de eficiencia del captador, las pérdidas en las tuberías, la energía acumulada en el agua que no alcanza la TADr y la mayor energía extraída del sistema en el agua producida. Para una TADr de 80 ºC, una parte importante de la energía permanece acumulada en el depósito sin alcanzar la TADr al final del día. Para aprovechar esta energía sería necesario disponer de un sistema complementario de suministro, ya que las pérdidas de calor nocturnas en el depósito pueden reducir considerablemente la energía útil disponible al día siguiente. La utilización del sistema solar como sistema único de suministro es inviable en la mayoría de los casos, especialmente a TADr elevadas, al no ajustarse la demanda de agua caliente a la estacionalidad de la producción del sistema solar, y al existir muchos días sin producción de agua caliente por la ausencia de irradiación mínima. Por el contrario, la inversión del sistema solar como sistema complementario para suministrar parte de la demanda térmica de una instalación es altamente recomendable. La energía útil anual del sistema solar estimada oscila entre 1322 kWh m-2 y 1084 kWh m-2. La mayor rentabilidad se obtendría suponiendo la existencia de una caldera eléctrica, donde la inversión se recuperaría en pocos años -entre 5.7 años a 40 ºC y 7.2 años a 80 ºC -. La rentabilidad también es elevada suponiendo la existencia de una caldera de gasóleo, con periodos de recuperación inferiores a 10 años. En una industria ficticia con demanda de 100 kWh d-1 y caldera de gasóleo existente, la inversión en una instalación solar optimizada sería rentable a cualquier TADr, con valores de VAN cercanos a la inversión realizada -12000 € a 80 ºC y 15000€ a 40 ºC- y un plazo de recuperación de la inversión entre 8 y 10 años. Los resultados de este estudio pueden ser de gran utilidad a la hora de determinar la viabilidad de utilización de sistemas similares para suministrar la demanda de agua caliente de agroindustrias y explotaciones agropecuarias, o para otras aplicaciones en las que se demande agua a temperaturas distintas de la habitual en uso doméstico (60 ºC). En cada caso, los rendimientos y la rentabilidad vendrán determinados por la irradiación de la zona, la temperatura del agua requerida y la curva de demanda de los procesos específicos. ABSTRACT The aim of this thesis is to contribute to the development and use of solar energy as an alternative for producing hot water in the agribusiness sector. Hot water supply is a key issue for a great many agribusinesses and agricultural holdings. Both hot water demand times and required tank water temperature (rTWT) are highly variable, where the demand profile tends to differ from domestic use. Further research is needed on how differences in rTWT influence the performance and feasibility of these systems. The main objective of this thesis is to characterize the performance and test the feasibility of an evacuated tube collector (ETC) solar water heating (SWH) system providing water at a higher temperature than is usual for such systems. The aim is to determine what influence the rTWT has on the system’s energy efficiency, quantify the volume of hot water that the system is capable of supplying at the respective rTWT and establish whether SWH is feasible as a booster supply system for the different analysed rTWTs. To do this, a prototype water heating system has been designed, installed and commissioned and its performance monitored at different rTWTs under real operating conditions. The quantitative results show that a higher rTWT results in a lower energy supply to the tank, where the differences may be greater than 1000 Wh m-2 d-1 from 40 ºC to 80 ºC for insolation values of around 8000 Wh m-2 d-1 (system efficiency ranges from 73% to 56%). The drop in supply is due to lower collector efficiency and greater heat losses from the pipe system. As regards water supplied at the rTWT, the insolation required for the first withdrawal of water to take place is greater at higher rTWTs, where the time between withdrawals increases and the number of withdrawals decreases throughout the day. As rTWT increases, the volume of water supplied at the rTWT decreases due to factors such as lower collector efficiency, pipe system heat losses, energy stored in the water at below the rTWT and more energy being extracted from the system by water heating. For a rTWT of 80 ºC, much of the energy is stored in the tank at below the rTWT at the end of the day. A booster supply system would be required to take advantage of this energy, as overnight tank heat losses may significantly reduce the usable energy available on the following day. It is often not feasible to use the solar system as a single supply system, especially at high rTWTs, as, unlike the supply from the solar heating system which does not produce hot water on many days of the year because insolation is below the required minimum, hot water demand is not seasonal. On the other hand, investment in a solar system as a booster system to meet part of a plant’s heat energy demand is highly recommended. The solar system’s estimated annual usable energy ranges from 1322 kWh m-2 to 1084 kWh m-2. Cost efficiency would be greatest if there were an existing electric boiler, where the payback period would be just a few years —from 5.7 years at 40 ºC to 7.2 years at 80 ºC—. Cost efficiency is also high if there is an existing diesel boiler with payback periods of under 10 years. In a fictitious industry with a demand of 100 kWh day-1 and an existing diesel boiler, the investment in the solar plant would be highly recommended at any rTWT, with a net present value similar to investment costs —12000 € at 80 ºC and 15000 € at 40 ºC— and a payback period of 10 years. The results of this study are potentially very useful for determining the feasibility of using similar systems for meeting the hot water demand of agribusinesses and arable and livestock farms or for other applications demanding water at temperatures not typical of domestic demand (60ºC). Performance and cost efficiency will be determined by the regional insolation, the required water temperature and the demand curve of the specific processes in each case.

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With the final goal of integrating III-V materials on silicon substrates for tandem solar cells, the influence of the Metal-Organic Vapor Phase Epitaxy (MOVPE) environment on the minority carrier properties of silicon wafers has been evaluated. These properties will essentially determine the photovoltaic performance of the bottom cell in a III-V-on-Si tandem solar cell. A comparison of the base minority carrier lifetimes obtained for different thermal processes carried out in a MOVPE reactor on Czochralski silicon wafers has been carried out. An important degradation of minority carrier lifetime during the surface preparation (i.e. H2 anneal) has been observed. Three different mechanisms have been proposed for explaining this behavior: 1) the introduction of extrinsic impurities coming from the reactor; 2) the activation of intrinsic lifetime killing impurities coming from the wafer itself; and finally, 3) the formation of crystal defects, which eventually become recombination centers. The effect of the emitter formation by phosphorus diffusion has also been evaluated. In this sense, it has been reported that lifetime can be recovered during the emitter formation either by the effect of the P on extracting impurities, or by the role of the atomic hydrogen on passivating the defects.

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"Work Performed Under Contract No. AC02-77CH00178."

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The status of silicon sheet development for photovoltaic applications is critically reviewed. Silicon sheet growth processes are classified according to their linear growth rates. The "fast" growth processes, which include edge-defined film-fed growth, silicon on ceramic, dendritic-web growth, and ribbon-to-ribbon growth, are comparatively ranked subject to criteria involving growth stability, sheet productivity, impurity effects, crystallinity, and solar cell results. The status of more rapid silicon ribbon growth techniques, such as horizontal ribbon growth and melt quenching, is also reviewed. The emphasis of the discussions is on examining the viability of these sheet materials as solar cell substrates for low-cost silicon photovoltaic systems.

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"Contract No. 954471 under NAS 7-100 SRI Project PYU 4980."