Energetic performance of landfill and digester biogas in a domestic cooker

The energetic performance of landfill biogas (LB) and biodigester biogas (BB) from municipal waste was examined in consumption tests. These tests were performed in situ at a gas generation plant associated with a landfill facility in Madrid (Spain) and following the standard UNE-EN 30-2-1 (1999). The jets of a domestic cooker commonly used for natural gas (NG) or liquefied petroleum gas (LPG) were modified to operate with the biogases produced at the facility. The working pressures best suited to the tested gases, i.e., to avoid flashback and flame lift, and to ensure the stability and correct functioning of the flame during combustion, were determined by trial and error. Both biogases returned optimum energetic performance for the transfer of heat to water in a metallic recipient (as required by the above standard) at a supply pressure of 10 mbar. Domestic cookers are normally supplied with NG at a pressure of 20 mbar, at which pressure the energetic performance of G20 reference gas was higher than that of both biogases (52.84% compared to 38.06% and 49.77% respectively). Data concerning these issues involving also unexplored feedstock are required for the correct conversions of domestic cookers in order to avoid risks of serious personal injuries or property damages.

Life cycle assessment as a policy-support tool: the case of taxis in the city of Madrid

This paper examined the potentialities of Life Cycle Assessment (LCA) as instrument for policy-support. To this respect, the adoption of an initiative within the Madrid Air Quality Plan (AQP) 2011–2015 regarding the substitution of diesel taxis with hybrid, natural gas and LPG alternatives was studied. Four different scenarios were elaborated, a business-as-usual scenario (BAU), the scenario of the AQP, and two extreme-situation scenarios: all-diesel (ADI) and all-ecologic (AEC). Impacts were characterized according to the ILCD methodology, focusing especially on climate change (CC) and photochemical ozone formation (PO). SimaPro 7.3 was used as analysis and inventory-construction tool. The results indicate that the shift to ecologic alternatives reduced impacts, especially those related to CC and PO. For the complete life cycle, reductions of 13% (CC) and 25% (PO) were observed for AQP against BAU (CC:1365 GgCO2, PO:13336 MgNMVOC). Deeper reductions were observed for AEC (CC:34%, PO:59%), while ADI produced slight increases in impacts if against BAU. The analysis of the use-phase revealed that the central and highest speed zones of the city benefit from the adoption of AQP. This is especially evident in zone 7, with reductions of 16% in CC and 31% in PO respectively against BAU (CCzone1:3443 kgCO2/veh·km, POzone7:11.1 kgNMVOC/veh·km).

Unidad de deshidratación y unidad DOMGAS. Planta de licuación Gorgon LNG

In this Project, a preliminary design of a dehydration unit for domestic gas will be outlined. This unit that is the subject of the study belongs to a project named Gorgon. Such project is currently been developed by Chevron in Barrow Island, Australia. In order to conduct a proper design of such unit, characteristics of the natural gas that is being extracted shall be detailed, as well as proper specifications of the pipeline to which the gas will supply. After this, different techniques for dehydrating the gas are evaluated; the technique that fits better this Project is absorption by glycol and following such assumption will be chosen as the best one. More accurately, the most suitable type of glycol for this particular unit is triethilene glycol, considering that it fits better the conditions of the project. Once the method is chosen, a simulation shall be undertaken with the purpose of determining the number of stages required for the correct functioning of the unit, the glycol rate and its purity. Besides, it is needed to estimate its pressure and temperature and the dimensions that would then follow. In addition, pressures and temperatures are estimated at the regeneration glycol process, together with dimensions of some units. Furthermore, it is necessary to estimate pressure and temperature at which natural gas is leaving the dehydration unit. In addition, both compression needed to secure the flux at the pipeline and the resulting pressure at the reception shall be studied. Finally, an economic study is carried out in order to conclude whether or not this specific Project is feasible.

Planta de licuación de 1 MTPA LNG Prico en Texas, EEUU

En este proyecto se ha realizado el dimensionamiento de los equipos básicos de una planta de licuación de gas natural cuya localización es Texas, EEUU. La capacidad de la planta es de 1 MTPA y funciona mediante un proceso de licuefacción de licencia Prico. Su objetivo fundamental es servir de apoyo en las puntas de consumo de gas natural (el cual varía considerablemente según la época del año) mediante reinyección del producto en los gaseoductos en los momentos de mayor demanda o incluso mediante su transporte en camiones cisterna. El proyecto ha comprendido el análisis del proceso Prico con su diagrama de flujo, el dimensionamiento de los intercambiadores de calor (carcasa y tubos y plate-fin), selección de los equipos rotativos, simulación del proceso y dimensionamiento de tuberías, así como un pequeño estudio económico. Abstract In this project, sizing of main equipment of a natural gas liquefaction plant has been developed. The plant is located in Texas, EEUU. Plant capacity is 1 MTPA and is designed to produce LNG by using a Prico liquefaction process. The main objective of the designed plant is to support the peaks of consumption of natural gas (which varies considerably along the year) by liquefying, storing and reinjecting the natural gas in the pipelines or even using tanker trucks to take LNG to consumers. The project includes the analysis of the Prico process flow diagram, sizing of the heat exchangers (shell & tube and plate-fin), selection of rotatory equipment, process simulation and pipe sizing, and a viability analysis.

Experimental and statistical investigation of canonical problems in sloshing

En hidrodinámica, el fenómeno de Sloshing se puede definir como el movimiento de la superficie libre de un fluido dentro de un contenedor sometido a fuerzas y perturbaciones externas. El fluido en cuestión experimenta violentos movimientos con importantes deformaciones de su superficie libre. La dinámica del fluido puede llegar a generar cargas hidrodinámicas considerables las cuales pueden afectar la integridad estructural y/o comprometer la estabilidad del vehículo que transporta dicho contenedor. El fenómeno de Sloshing ha sido extensivamente investigado matemática, numérica y experimentalmente, siendo el enfoque experimental el más usado debido a la complejidad del problema, para el cual los modelos matemáticos y de simulación son aun incapaces de predecir con suficiente rapidez y precisión las cargas debidas a dicho fenómeno. El flujo generado por el Sloshing usualmente se caracteriza por la presencia de un fluido multifase (gas-liquido) y turbulencia. Reducir al máximo posible la complejidad del fenómeno de Sloshing sin perder la esencia del problema es el principal reto de esta tesis doctoral, donde un trabajo experimental enfocado en casos canónicos de Sloshing es presentado y documentado con el objetivo de aumentar la comprensión de dicho fenómeno y por tanto intentar proveer información valiosa para validaciones de códigos numéricos. El fenómeno de Sloshing juega un papel importante en la industria del transporte marítimo de gas licuado (LNG). El mercado de LNG en los últimos años ha reportado un crecimiento hasta tres veces mayor al de los mercados de petróleo y gas convencionales. Ingenieros en laboratorios de investigación e ingenieros adscritos a la industria del LNG trabajan continuamente buscando soluciones económicas y seguras para contener, transferir y transportar grandes volúmenes de LNG. Los buques transportadores de LNG (LNGC) han pasado de ser unos pocos buques con capacidad de 75000 m3 hace unos treinta años, a una amplia flota con una capacidad de 140000 m3 actualmente. En creciente número, hoy día se construyen buques con capacidades que oscilan entre 175000 m3 y 250000 m3. Recientemente un nuevo concepto de buque LNG ha salido al mercado y se le conoce como FLNG. Un FLNG es un buque de gran valor añadido que solventa los problemas de extracción, licuefacción y almacenamiento del LNG, ya que cuenta con equipos de extracción y licuefacción a bordo, eliminando por tanto las tareas de transvase de las estaciones de licuefacción en tierra hacia los buques LNGC. EL LNG por tanto puede ser transferido directamente desde el FLNG hacia los buques LNGC en mar abierto. Niveles de llenado intermedios en combinación con oleaje durante las operaciones de trasvase inducen movimientos en los buques que generan por tanto el fenómeno de Sloshing dentro de los tanques de los FLNG y los LNGC. El trabajo de esta tesis doctoral lidia con algunos de los problemas del Sloshing desde un punto de vista experimental y estadístico, para ello una serie de tareas, descritas a continuación, se han llevado a cabo : 1. Un dispositivo experimental de Sloshing ha sido configurado. Dicho dispositivo ha permitido ensayar secciones rectangulares de tanques LNGC a escala con movimientos angulares de un grado de libertad. El dispositivo experimental ha sido instrumentado para realizar mediciones de movimiento, presiones, vibraciones y temperatura, así como la grabación de imágenes y videos. 2. Los impactos de olas generadas dentro de una sección rectangular de un LNGC sujeto a movimientos regulares forzados han sido estudiados mediante la caracterización del fenómeno desde un punto de vista estadístico enfocado en la repetitividad y la ergodicidad del problema. 3. El estudio de los impactos provocados por movimientos regulares ha sido extendido a un escenario más realístico mediante el uso de movimientos irregulares forzados. 4. El acoplamiento del Sloshing generado por el fluido en movimiento dentro del tanque LNGC y la disipación de la energía mecánica de un sistema no forzado de un grado de libertad (movimiento angular) sujeto a una excitación externa ha sido investigado. 5. En la última sección de esta tesis doctoral, la interacción entre el Sloshing generado dentro en una sección rectangular de un tanque LNGC sujeto a una excitación regular y un cuerpo elástico solidario al tanque ha sido estudiado. Dicho estudio corresponde a un problema de interacción fluido-estructura. Abstract In hydrodynamics, we refer to sloshing as the motion of liquids in containers subjected to external forces with large free-surface deformations. The liquid motion dynamics can generate loads which may affect the structural integrity of the container and the stability of the vehicle that carries such container. The prediction of these dynamic loads is a major challenge for engineers around the world working on the design of both the container and the vehicle. The sloshing phenomenon has been extensively investigated mathematically, numerically and experimentally. The latter has been the most fruitful so far, due to the complexity of the problem, for which the numerical and mathematical models are still incapable of accurately predicting the sloshing loads. The sloshing flows are usually characterised by the presence of multiphase interaction and turbulence. Reducing as much as possible the complexity of the sloshing problem without losing its essence is the main challenge of this phd thesis, where experimental work on selected canonical cases are presented and documented in order to better understand the phenomenon and to serve, in some cases, as an useful information for numerical validations. Liquid sloshing plays a key roll in the liquified natural gas (LNG) maritime transportation. The LNG market growth is more than three times the rated growth of the oil and traditional gas markets. Engineers working in research laboratories and companies are continuously looking for efficient and safe ways for containing, transferring and transporting the liquified gas. LNG carrying vessels (LNGC) have evolved from a few 75000 m3 vessels thirty years ago to a huge fleet of ships with a capacity of 140000 m3 nowadays and increasing number of 175000 m3 and 250000 m3 units. The concept of FLNG (Floating Liquified Natural Gas) has appeared recently. A FLNG unit is a high value-added vessel which can solve the problems of production, treatment, liquefaction and storage of the LNG because the vessel is equipped with a extraction and liquefaction facility. The LNG is transferred from the FLNG to the LNGC in open sea. The combination of partial fillings and wave induced motions may generate sloshing flows inside both the LNGC and the FLNG tanks. This work has dealt with sloshing problems from a experimental and statistical point of view. A series of tasks have been carried out: 1. A sloshing rig has been set up. It allows for testing tanks with one degree of freedom angular motion. The rig has been instrumented to measure motions, pressure and conduct video and image recording. 2. Regular motion impacts inside a rectangular section LNGC tank model have been studied, with forced motion tests, in order to characterise the phenomenon from a statistical point of view by assessing the repeatability and practical ergodicity of the problem. 3. The regular motion analysis has been extended to an irregular motion framework in order to reproduce more realistic scenarios. 4. The coupled motion of a single degree of freedom angular motion system excited by an external moment and affected by the fluid moment and the mechanical energy dissipation induced by sloshing inside the tank has been investigated. 5. The last task of the thesis has been to conduct an experimental investigation focused on the strong interaction between a sloshing flow in a rectangular section of a LNGC tank subjected to regular excitation and an elastic body clamped to the tank. It is thus a fluid structure interaction problem.

Environmental analysis of a Concentrated Solar Power (CSP) plant hybridised with different fossil and renewable fuels

The environmental performance of a 50 MW parabolic trough Concentrated Solar Power (CSP) plant hybridised with different fuels was determined using a Life Cycle Assessment methodology. Six different scenarios were investigated, half of which involved hybridisation with fossil fuels (natural gas, coal and fuel oil), and the other three involved hybridisation with renewable fuels (wheat straw, wood pellets and biogas). Each scenario was compared to a solar-only operation. Nine different environmental categories as well as the Cumulative Energy Demand and the Energy Payback Time (EPT) were evaluated using Simapro software for 1 MWh of electricity produced. The results indicate a worse environmental performance for a CSP plant producing 12% of the electricity from fuel than in a solar-only operation for every indicator, except for the eutrophication and toxicity categories, whose results for the natural gas scenario are slightly better. In the climate change category, the results ranged between 26.9 and 187 kg CO2 eq/MWh, where a solar-only operation had the best results and coal hybridisation had the worst. Considering a weighted single score indicator, the environmental impact of the renewable fuels scenarios is approximately half of those considered in fossil fuels, with the straw scenario showing the best results, and the coal scenario the worstones. EPT for solar-only mode is 1.44 years, while hybridisation scenarios EPT vary in a range of 1.72 -1.83 years for straw and pellets respectively. The fuels with more embodied energy are biomethane and wood pellets.

Evaluación de las Consecuencias de la Nueva Regulación de la OMI sobre Combustibles Marinos

El 10 de octubre de 2008 la Organización Marítima Internacional (OMI) firmó una modificación al Anexo VI del convenio MARPOL 73/78, por la que estableció una reducción progresiva de las emisiones de óxidos de azufre (SOx) procedentes de los buques, una reducción adicional de las emisiones de óxidos de nitrógeno (NOx), así como límites en las emisiones de dióxido de Carbono (CO2) procedentes de los motores marinos y causantes de problemas medioambientales como la lluvia ácida y efecto invernadero. Centrándonos en los límites sobre las emisiones de azufre, a partir del 1 de enero de 2015 esta normativa obliga a todos los buques que naveguen por zonas controladas, llamadas Emission Control Area (ECA), a consumir combustibles con un contenido de azufre menor al 0,1%. A partir del 1 de enero del año 2020, o bien del año 2025, si la OMI decide retrasar su inicio, los buques deberán consumir combustibles con un contenido de azufre menor al 0,5%. De igual forma que antes, el contenido deberá ser rebajado al 0,1%S, si navegan por el interior de zonas ECA. Por su parte, la Unión Europea ha ido más allá que la OMI, adelantando al año 2020 la aplicación de los límites más estrictos de la ley MARPOL sobre las aguas de su zona económica exclusiva. Para ello, el 21 de noviembre de 2013 firmó la Directiva 2012 / 33 / EU como adenda a la Directiva de 1999. Tengamos presente que la finalidad de estas nuevas leyes es la mejora de la salud pública y el medioambiente, produciendo beneficios sociales, en forma de reducción de enfermedades, sobre todo de tipo respiratorio, a la vez que se reduce la lluvia ácida y sus nefastas consecuencias. La primera pregunta que surge es ¿cuál es el combustible actual de los buques y cuál será el que tengan que consumir para cumplir con esta Regulación? Pues bien, los grandes buques de navegación internacional consumen hoy en día fuel oil con un nivel de azufre de 3,5%. ¿Existen fueles con un nivel de azufre de 0,5%S? Como hemos concluido en el capítulo 4, para las empresas petroleras, la producción de fuel oil como combustible marino es tratada como un subproducto en su cesta de productos refinados por cada barril de Brent, ya que la demanda de fuel respecto a otros productos está bajando y además, el margen de beneficio que obtienen por la venta de otros productos petrolíferos es mayor que con el fuel. Así, podemos decir que las empresas petroleras no están interesadas en invertir en sus refinerías para producir estos fueles con menor contenido de azufre. Es más, en el caso de que alguna compañía decidiese invertir en producir un fuel de 0,5%S, su precio debería ser muy similar al del gas��leo para poder recuperar las inversiones empleadas. Por lo tanto, el único combustible que actualmente cumple con los nuevos niveles impuestos por la OMI es el gas��leo, con un precio que durante el año 2014 estuvo a una media de 307 USD/ton más alto que el actual fuel oil. Este mayor precio de compra de combustible impactará directamente sobre el coste del trasporte marítimo. La entrada en vigor de las anteriores normativas está suponiendo un reto para todo el sector marítimo. Ante esta realidad, se plantean diferentes alternativas con diferentes implicaciones técnicas, operativas y financieras. En la actualidad, son tres las alternativas con mayor aceptación en el sector. La primera alternativa consiste en “no hacer nada” y simplemente cambiar el tipo de combustible de los grandes buques de fuel oil a gas��leo. Las segunda alternativa es la instalación de un equipo scrubber, que permitiría continuar con el consumo de fuel oil, limpiando sus gases de combustión antes de salir a la atmósfera. Y, por último, la tercera alternativa consiste en el uso de Gas Natural Licuado (GNL) como combustible, con un precio inferior al del gas��leo. Sin embargo, aún existen importantes incertidumbres sobre la evolución futura de precios, operación y mantenimiento de las nuevas tecnologías, inversiones necesarias, disponibilidad de infraestructura portuaria e incluso el desarrollo futuro de la propia normativa internacional. Estas dudas hacen que ninguna de estas tres alternativas sea unánime en el sector. En esta tesis, tras exponer en el capítulo 3 la regulación aplicable al sector, hemos investigado sus consecuencias. Para ello, hemos examinado en el capítulo 4 si existen en la actualidad combustibles marinos que cumplan con los nuevos límites de azufre o en su defecto, cuál sería el precio de los nuevos combustibles. Partimos en el capítulo 5 de la hipótesis de que todos los buques cambian su consumo de fuel oil a gas��leo para cumplir con dicha normativa, calculamos el incremento de demanda de gas��leo que se produciría y analizamos las consecuencias que este hecho tendría sobre la producción de gas��leos en el Mediterráneo. Adicionalmente, calculamos el impacto económico que dicho incremento de coste producirá sobre sector exterior de España. Para ello, empleamos como base de datos el sistema de control de tráfico marítimo Authomatic Identification System (AIS) para luego analizar los datos de todos los buques que han hecho escala en algún puerto español, para así calcular el extra coste anual por el consumo de gas��leo que sufrirá el transporte marítimo para mover todas las importaciones y exportaciones de España. Por último, en el capítulo 6, examinamos y comparamos las otras dos alternativas al consumo de gas��leo -scrubbers y propulsión con GNL como combustible- y, finalmente, analizamos en el capítulo 7, la viabilidad de las inversiones en estas dos tecnologías para cumplir con la regulación. En el capítulo 5 explicamos los numerosos métodos que existen para calcular la demanda de combustible de un buque. La metodología seguida para su cálculo será del tipo bottom-up, que está basada en la agregación de la actividad y las características de cada tipo de buque. El resultado está basado en la potencia instalada de cada buque, porcentaje de carga del motor y su consumo específico. Para ello, analizamos el número de buques que navegan por el Mediterráneo a lo largo de un año mediante el sistema AIS, realizando “fotos” del tráfico marítimo en el Mediterráneo y reportando todos los buques en navegación en días aleatorios a lo largo de todo el año 2014. Por último, y con los datos anteriores, calculamos la demanda potencial de gas��leo en el Mediterráneo. Si no se hace nada y los buques comienzan a consumir gas��leo como combustible principal, en vez del actual fuel oil para cumplir con la regulación, la demanda de gasoil en el Mediterráneo aumentará en 12,12 MTA (Millones de Toneladas Anuales) a partir del año 2020. Esto supone alrededor de 3.720 millones de dólares anuales por el incremento del gasto de combustible tomando como referencia el precio medio de los combustibles marinos durante el año 2014. El anterior incremento de demanda en el Mediterráneo supondría el 43% del total de la demanda de gas��leos en España en el año 2013, incluyendo gas��leos de automoción, biodiesel y gas��leos marinos y el 3,2% del consumo europeo de destilados medios durante el año 2014. ¿Podrá la oferta del mercado europeo asumir este incremento de demanda de gas��leos? Europa siempre ha sido excedentaria en gasolina y deficitaria en destilados medios. En el año 2009, Europa tuvo que importar 4,8 MTA de Norte América y 22,1 MTA de Asia. Por lo que, este aumento de demanda sobre la ya limitada capacidad de refino de destilados medios en Europa incrementará las importaciones y producirá también aumentos en los precios, sobre todo del mercado del gas��leo. El sector sobre el que más impactará el incremento de demanda de gas��leo será el de los cruceros que navegan por el Mediterráneo, pues consumirán un 30,4% de la demanda de combustible de toda flota mundial de cruceros, lo que supone un aumento en su gasto de combustible de 386 millones de USD anuales. En el caso de los RoRos, consumirían un 23,6% de la demanda de la flota mundial de este tipo de buque, con un aumento anual de 171 millones de USD sobre su gasto de combustible anterior. El mayor incremento de coste lo sufrirán los portacontenedores, con 1.168 millones de USD anuales sobre su gasto actual. Sin embargo, su consumo en el Mediterráneo representa sólo el 5,3% del consumo mundial de combustible de este tipo de buques. Estos números plantean la incertidumbre de si semejante aumento de gasto en buques RoRo hará que el transporte marítimo de corta distancia en general pierda competitividad sobre otros medios de transporte alternativos en determinadas rutas. De manera que, parte del volumen de mercancías que actualmente transportan los buques se podría trasladar a la carretera, con los inconvenientes medioambientales y operativos, que esto produciría. En el caso particular de España, el extra coste por el consumo de gas��leo de todos los buques con escala en algún puerto español en el año 2013 se cifra en 1.717 millones de EUR anuales, según demostramos en la última parte del capítulo 5. Para realizar este cálculo hemos analizado con el sistema AIS a todos los buques que han tenido escala en algún puerto español y los hemos clasificado por distancia navegada, tipo de buque y potencia. Este encarecimiento del transporte marítimo será trasladado al sector exterior español, lo cual producirá un aumento del coste de las importaciones y exportaciones por mar en un país muy expuesto, pues el 75,61% del total de las importaciones y el 53,64% del total de las exportaciones se han hecho por vía marítima. Las tres industrias que se verán más afectadas son aquellas cuyo valor de mercancía es inferior respecto a su coste de transporte. Para ellas los aumentos del coste sobre el total del valor de cada mercancía serán de un 2,94% para la madera y corcho, un 2,14% para los productos minerales y un 1,93% para las manufacturas de piedra, cemento, cerámica y vidrio. Las mercancías que entren o salgan por los dos archipiélagos españoles de Canarias y Baleares serán las que se verán más impactadas por el extra coste del transporte marítimo, ya que son los puertos más alejados de otros puertos principales y, por tanto, con más distancia de navegación. Sin embargo, esta no es la única alternativa al cumplimiento de la nueva regulación. De la lectura del capítulo 6 concluimos que las tecnologías de equipos scrubbers y de propulsión con GNL permitirán al buque consumir combustibles más baratos al gasoil, a cambio de una inversión en estas tecnologías. ¿Serán los ahorros producidos por estas nuevas tecnologías suficientes para justificar su inversión? Para contestar la anterior pregunta, en el capítulo 7 hemos comparado las tres alternativas y hemos calculado tanto los costes de inversión como los gastos operativos correspondientes a equipos scrubbers o propulsión con GNL para una selección de 53 categorías de buques. La inversión en equipos scrubbers es más conveniente para buques grandes, con navegación no regular. Sin embargo, para buques de tamaño menor y navegación regular por puertos con buena infraestructura de suministro de GNL, la inversión en una propulsión con GNL como combustible será la más adecuada. En el caso de un tiempo de navegación del 100% dentro de zonas ECA y bajo el escenario de precios visto durante el año 2014, los proyectos con mejor plazo de recuperación de la inversión en equipos scrubbers son para los cruceros de gran tamaño (100.000 tons. GT), para los que se recupera la inversión en 0,62 años, los grandes portacontenedores de más de 8.000 TEUs con 0,64 años de recuperación y entre 5.000-8.000 TEUs con 0,71 años de recuperación y, por último, los grandes petroleros de más de 200.000 tons. de peso muerto donde tenemos un plazo de recuperación de 0,82 años. La inversión en scrubbers para buques pequeños, por el contrario, tarda más tiempo en recuperarse llegando a más de 5 años en petroleros y quimiqueros de menos de 5.000 toneladas de peso muerto. En el caso de una posible inversión en propulsión con GNL, las categorías de buques donde la inversión en GNL es más favorable y recuperable en menor tiempo son las más pequeñas, como ferris, cruceros o RoRos. Tomamos ahora el caso particular de un buque de productos limpios de 38.500 toneladas de peso muerto ya construido y nos planteamos la viabilidad de la inversión en la instalación de un equipo scrubber o bien, el cambio a una propulsión por GNL a partir del año 2015. Se comprueba que las dos variables que más impactan sobre la conveniencia de la inversión son el tiempo de navegación del buque dentro de zonas de emisiones controladas (ECA) y el escenario futuro de precios del MGO, HSFO y GNL. Para realizar este análisis hemos estudiado cada inversión, calculando una batería de condiciones de mérito como el payback, TIR, VAN y la evolución de la tesorería del inversor. Posteriormente, hemos calculado las condiciones de contorno mínimas de este buque en concreto para asegurar una inversión no sólo aceptable, sino además conveniente para el naviero inversor. En el entorno de precios del 2014 -con un diferencial entre fuel y gas��leo de 264,35 USD/ton- si el buque pasa más de un 56% de su tiempo de navegación en zonas ECA, conseguirá una rentabilidad de la inversión para inversores (TIR) en el equipo scrubber que será igual o superior al 9,6%, valor tomado como coste de oportunidad. Para el caso de inversión en GNL, en el entorno de precios del año 2014 -con un diferencial entre GNL y gas��leo de 353,8 USD/ton FOE- si el buque pasa más de un 64,8 % de su tiempo de navegación en zonas ECA, conseguirá una rentabilidad de la inversión para inversores (TIR) que será igual o superior al 9,6%, valor del coste de oportunidad. Para un tiempo en zona ECA estimado de un 60%, la rentabilidad de la inversión (TIR) en scrubbers para los inversores será igual o superior al 9,6%, el coste de oportunidad requerido por el inversor, para valores del diferencial de precio entre los dos combustibles alternativos, gas��leo (MGO) y fuel oil (HSFO) a partir de 244,73 USD/ton. En el caso de una inversión en propulsión GNL se requeriría un diferencial de precio entre MGO y GNL de 382,3 USD/ton FOE o superior. Así, para un buque de productos limpios de 38.500 DWT, la inversión en una reconversión para instalar un equipo scrubber es más conveniente que la de GNL, pues alcanza rentabilidades de la inversión (TIR) para inversores del 12,77%, frente a un 6,81% en el caso de invertir en GNL. Para ambos cálculos se ha tomado un buque que navegue un 60% de su tiempo por zona ECA y un escenario de precios medios del año 2014 para el combustible. Po otro lado, las inversiones en estas tecnologías a partir del año 2025 para nuevas construcciones son en ambos casos convenientes. El naviero deberá prestar especial atención aquí a las características propias de su buque y tipo de navegación, así como a la infraestructura de suministros y vertidos en los puertos donde vaya a operar usualmente. Si bien, no se ha estudiado en profundidad en esta tesis, no olvidemos que el sector marítimo debe cumplir además con las otras dos limitaciones que la regulación de la OMI establece sobre las emisiones de óxidos de Nitrógeno (NOx) y Carbono (CO2) y que sin duda, requerirán adicionales inversiones en diversos equipos. De manera que, si bien las consecuencias del consumo de gas��leo como alternativa al cumplimiento de la Regulación MARPOL son ciertamente preocupantes, existen alternativas al uso del gas��leo, con un aumento sobre el coste del transporte marítimo menor y manteniendo los beneficios sociales que pretende dicha ley. En efecto, como hemos demostrado, las opciones que se plantean como más rentables desde el punto de vista financiero son el consumo de GNL en los buques pequeños y de línea regular (cruceros, ferries, RoRos), y la instalación de scrubbers para el resto de buques de grandes dimensiones. Pero, por desgracia, estas inversiones no llegan a hacerse realidad por el elevado grado de incertidumbre asociado a estos dos mercados, que aumenta el riesgo empresarial, tanto de navieros como de suministradores de estas nuevas tecnologías. Observamos así una gran reticencia del sector privado a decidirse por estas dos alternativas. Este elevado nivel de riesgo sólo puede reducirse fomentando el esfuerzo conjunto del sector público y privado para superar estas barreras de entrada del mercado de scrubbers y GNL, que lograrían reducir las externalidades medioambientales de las emisiones sin restar competitividad al transporte marítimo. Creemos así, que los mismos organismos que aprobaron dicha ley deben ayudar al sector naviero a afrontar las inversiones en dichas tecnologías, así como a impulsar su investigación y promover la creación de una infraestructura portuaria adaptada a suministros de GNL y a descargas de vertidos procedentes de los equipos scrubber. Deberían además, prestar especial atención sobre las ayudas al sector de corta distancia para evitar que pierda competitividad frente a otros medios de transporte por el cumplimiento de esta normativa. Actualmente existen varios programas europeos de incentivos, como TEN-T o Marco Polo, pero no los consideramos suficientes. Por otro lado, la Organización Marítima Internacional debe confirmar cuanto antes si retrasa o no al 2025 la nueva bajada del nivel de azufre en combustibles. De esta manera, se eliminaría la gran incertidumbre temporal que actualmente tienen tanto navieros, como empresas petroleras y puertos para iniciar sus futuras inversiones y poder estudiar la viabilidad de cada alternativa de forma individual. ABSTRACT On 10 October 2008 the International Maritime Organization (IMO) signed an amendment to Annex VI of the MARPOL 73/78 convention establishing a gradual reduction in sulphur oxide (SOx) emissions from ships, and an additional reduction in nitrogen oxide (NOx) emissions and carbon dioxide (CO2) emissions from marine engines which cause environmental problems such as acid rain and the greenhouse effect. According to this regulation, from 1 January 2015, ships travelling in an Emission Control Area (ECA) must use fuels with a sulphur content of less than 0.1%. From 1 January 2020, or alternatively from 2025 if the IMO should decide to delay its introduction, all ships must use fuels with a sulphur content of less than 0.5%. As before, this content will be 0.1%S for voyages within ECAs. Meanwhile, the European Union has gone further than the IMO, and will apply the strictest limits of the MARPOL directives in the waters of its exclusive economic zone from 2020. To this end, Directive 2012/33/EU was issued on 21 November 2013 as an addendum to the 1999 Directive. These laws are intended to improve public health and the environment, benefiting society by reducing disease, particularly respiratory problems. The first question which arises is: what fuel do ships currently use, and what fuel will they have to use to comply with the Convention? Today, large international shipping vessels consume fuel oil with a sulphur level of 3.5%. Do fuel oils exist with a sulphur level of 0.5%S? As we conclude in Chapter 4, oil companies regard marine fuel oil as a by-product of refining Brent to produce their basket of products, as the demand for fuel oil is declining in comparison to other products, and the profit margin on the sale of other petroleum products is higher. Thus, oil companies are not interested in investing in their refineries to produce low-sulphur fuel oils, and if a company should decide to invest in producing a 0.5%S fuel oil, its price would have to be very similar to that of marine gas oil in order to recoup the investment. Therefore, the only fuel which presently complies with the new levels required by the IMO is marine gas oil, which was priced on average 307 USD/tonne higher than current fuel oils during 2014. This higher purchasing price for fuel will have a direct impact on the cost of maritime transport. The entry into force of the above directive presents a challenge for the entire maritime sector. There are various alternative approaches to this situation, with different technical, operational and financial implications. At present three options are the most widespread in the sector. The first option consists of “doing nothing” and simply switching from fuel oil to marine gas oil in large ships. The second option is installing a scrubber system, which would enable ships to continue consuming fuel oil, cleaning the combustion gases before they are released to the atmosphere. And finally, the third option is using Liquefied Natural Gas (LNG), which is priced lower than marine gas oil, as a fuel. However, there is still significant uncertainty on future variations in prices, the operation and maintenance of the new technologies, the investments required, the availability of port infrastructure and even future developments in the international regulations themselves. These uncertainties mean that none of these three alternatives has been unanimously accepted by the sector. In this Thesis, after discussing all the regulations applicable to the sector in Chapter 3, we investigate their consequences. In Chapter 4 we examine whether there are currently any marine fuels on the market which meet the new sulphur limits, and if not, how much new fuels would cost. In Chapter 5, based on the hypothesis that all ships will switch from fuel oil to marine gas oil to comply with the regulations, we calculate the increase in demand for marine gas oil this would lead to, and analyse the consequences this would have on marine gas oil production in the Mediterranean. We also calculate the economic impact such a cost increase would have on Spain's external sector. To do this, we also use the Automatic Identification System (AIS) system to analyse the data of every ship stopping in any Spanish port, in order to calculate the extra cost of using marine gas oil in maritime transport for all Spain's imports and exports. Finally, in Chapter 6, we examine and compare the other two alternatives to marine gas oil, scrubbers and LNG, and in Chapter 7 we analyse the viability of investing in these two technologies in order to comply with the regulations. In Chapter 5 we explain the many existing methods for calculating a ship's fuel consumption. We use a bottom-up calculation method, based on aggregating the activity and characteristics of each type of vessel. The result is based on the installed engine power of each ship, the engine load percentage and its specific consumption. To do this, we analyse the number of ships travelling in the Mediterranean in the course of one year, using the AIS, a marine traffic monitoring system, to take “snapshots” of marine traffic in the Mediterranean and report all ships at sea on random days throughout 2014. Finally, with the above data, we calculate the potential demand for marine gas oil in the Mediterranean. If nothing else is done and ships begin to use marine gas oil instead of fuel oil in order to comply with the regulation, the demand for marine gas oil in the Mediterranean will increase by 12.12 MTA (Millions Tonnes per Annum) from 2020. This means an increase of around 3.72 billion dollars a year in fuel costs, taking as reference the average price of marine fuels in 2014. Such an increase in demand in the Mediterranean would be equivalent to 43% of the total demand for diesel in Spain in 2013, including automotive diesel fuels, biodiesel and marine gas oils, and 3.2% of European consumption of middle distillates in 2014. Would the European market be able to supply enough to meet this greater demand for diesel? Europe has always had a surplus of gasoline and a deficit of middle distillates. In 2009, Europe had to import 4.8 MTA from North America and 22.1 MTA from Asia. Therefore, this increased demand on Europe's already limited capacity for refining middle distillates would lead to increased imports and higher prices, especially in the diesel market. The sector which would suffer the greatest impact of increased demand for marine gas oil would be Mediterranean cruise ships, which represent 30.4% of the fuel demand of the entire world cruise fleet, meaning their fuel costs would rise by 386 million USD per year. ROROs in the Mediterranean, which represent 23.6% of the demand of the world fleet of this type of ship, would see their fuel costs increase by 171 million USD a year. The greatest cost increase would be among container ships, with an increase on current costs of 1.168 billion USD per year. However, their consumption in the Mediterranean represents only 5.3% of worldwide fuel consumption by container ships. These figures raise the question of whether a cost increase of this size for RORO ships would lead to short-distance marine transport in general becoming less competitive compared to other transport options on certain routes. For example, some of the goods that ships now carry could switch to road transport, with the undesirable effects on the environment and on operations that this would produce. In the particular case of Spain, the extra cost of switching to marine gas oil in all ships stopping at any Spanish port in 2013 would be 1.717 billion EUR per year, as we demonstrate in the last part of Chapter 5. For this calculation, we used the AIS system to analyse all ships which stopped at any Spanish port, classifying them by distance travelled, type of ship and engine power. This rising cost of marine transport would be passed on to the Spanish external sector, increasing the cost of imports and exports by sea in a country which relies heavily on maritime transport, which accounts for 75.61% of Spain's total imports and 53.64% of its total exports. The three industries which would be worst affected are those with goods of lower value relative to transport costs. The increased costs over the total value of each good would be 2.94% for wood and cork, 2.14% for mineral products and 1.93% for manufactured stone, cement, ceramic and glass products. Goods entering via the two Spanish archipelagos, the Canary Islands and the Balearic Islands, would suffer the greatest impact from the extra cost of marine transport, as these ports are further away from other major ports and thus the distance travelled is greater. However, this is not the only option for compliance with the new regulations. From our readings in Chapter 6 we conclude that scrubbers and LNG propulsion would enable ships to use cheaper fuels than marine gas oil, in exchange for investing in these technologies. Would the savings gained by these new technologies be enough to justify the investment? To answer this question, in Chapter 7 we compare the three alternatives and calculate both the cost of investment and the operating costs associated with scrubbers or LNG propulsion for a selection of 53 categories of ships. Investing in scrubbers is more advisable for large ships with no fixed runs. However, for smaller ships with regular runs to ports with good LNG supply infrastructure, investing in LNG propulsion would be the best choice. In the case of total transit time within an ECA and the pricing scenario seen in 2014, the best payback periods on investments in scrubbers are for large cruise ships (100,000 gross tonnage), which would recoup their investment in 0.62 years; large container ships, with a 0.64 year payback period for those over 8,000 TEUs and 0.71 years for the 5,000-8,000 TEU category; and finally, large oil tankers over 200,000 deadweight tonnage, which would recoup their investment in 0.82 years. However, investing in scrubbers would have a longer payback period for smaller ships, up to 5 years or more for oil tankers and chemical tankers under 5,000 deadweight tonnage. In the case of LNG propulsion, a possible investment is more favourable and the payback period is shorter for smaller ship classes, such as ferries, cruise ships and ROROs. We now take the case of a ship transporting clean products, already built, with a deadweight tonnage of 38,500, and consider the viability of investing in installing a scrubber or changing to LNG propulsion, starting in 2015. The two variables with the greatest impact on the advisability of the investment are how long the ship is at sea within emission control areas (ECA) and the future price scenario of MGO, HSFO and LNG. For this analysis, we studied each investment, calculating a battery of merit conditions such as the payback period, IRR, NPV and variations in the investors' liquid assets. We then calculated the minimum boundary conditions to ensure the investment was not only acceptable but advisable for the investor shipowner. Thus, for the average price differential of 264.35 USD/tonne between HSFO and MGO during 2014, investors' return on investment (IRR) in scrubbers would be the same as the required opportunity cost of 9.6%, for values of over 56% ship transit time in ECAs. For the case of investing in LNG and the average price differential between MGO and LNG of 353.8 USD/tonne FOE in 2014, the ship must spend 64.8% of its time in ECAs for the investment to be advisable. For an estimated 60% of time in an ECA, the internal rate of return (IRR) for investors equals the required opportunity cost of 9.6%, based on a price difference of 244.73 USD/tonne between the two alternative fuels, marine gas oil (MGO) and fuel oil (HSFO). An investment in LNG propulsion would require a price differential between MGO and LNG of 382.3 USD/tonne FOE. Thus, for a 38,500 DWT ship carrying clean products, investing in retrofitting to install a scrubber is more advisable than converting to LNG, with an internal rate of return (IRR) for investors of 12.77%, compared to 6.81% for investing in LNG. Both calculations were based on a ship which spends 60% of its time at sea in an ECA and a scenario of average 2014 prices. However, for newly-built ships, investments in either of these technologies from 2025 would be advisable. Here, the shipowner must pay particular attention to the specific characteristics of their ship, the type of operation, and the infrastructure for supplying fuel and handling discharges in the ports where it will usually operate. Thus, while the consequences of switching to marine gas oil in order to comply with the MARPOL regulations are certainly alarming, there are alternatives to marine gas oil, with smaller increases in the costs of maritime transport, while maintaining the benefits to society this law is intended to provide. Indeed, as we have demonstrated, the options which appear most favourable from a financial viewpoint are conversion to LNG for small ships and regular runs (cruise ships, ferries, ROROs), and installing scrubbers for large ships. Unfortunately, however, these investments are not being made, due to the high uncertainty associated with these two markets, which increases business risk, both for shipowners and for the providers of these new technologies. This means we are seeing considerable reluctance regarding these two options among the private sector. This high level of risk can be lowered only by encouraging joint efforts by the public and private sectors to overcome these barriers to entry into the market for scrubbers and LNG, which could reduce the environmental externalities of emissions without affecting the competitiveness of marine transport. Our opinion is that the same bodies which approved this law must help the shipping industry invest in these technologies, drive research on them, and promote the creation of a port infrastructure which is adapted to supply LNG and handle the discharges from scrubber systems. At present there are several European incentive programmes, such as TEN-T and Marco Polo, but we do not consider these to be sufficient. For its part, the International Maritime Organization should confirm as soon as possible whether the new lower sulphur levels in fuels will be postponed until 2025. This would eliminate the great uncertainty among shipowners, oil companies and ports regarding the timeline for beginning their future investments and for studying their viability.

Discourses and values underpin public debate on fracking in Spain: a case study at the crossroad

In the EU context extraction of shale and oil gas by hydraulic fracturing (fracking) differs from country to country in terms of legislation and implementation. While fossil fuel extraction using this technology is currently taking place in the UK, Germany and France have adopted respective moratoria. In between is the Spanish case, where hydrocarbon extraction projects through fracking have to undergo mandatory and routine environmental assessment in accordance with the last changes to environmental regulations. Nowadays Spain is at the crossroad with respect to the future of this technology. We presume a social conflictt in our country since the position and strategy of the involved and confronted social actors -national, regional and local authorities, energy companies, scientists, NGO and other social organization- are going to play key and likely divergent roles in its industrial implementation and public acceptance. In order to improve knowledge on how to address these controverted situations from the own engineering context, the affiliated units from the Higher Technical School of Mines and Energy Engineering at UPM have been working on a transversal program to teach values and ethics. Over the past seven years, this pioneering experience has shown the usefulness of applying a consequentialist ethics, based on a case-by-case approach and costs-benefits analysis both for action and inaction. As a result of this initiative a theoretical concept has arisen and crystallized in this field: it is named Inter-ethics. This theoretical perspective can be very helpful in complex situations, with multi-stakeholders and plurality of interests, when ethical management requires the interaction between the respective ethics of each group; professional ethics of a single group is not enough. Under this inter-ethics theoretical framework and applying content analysis techniques, this paper explores the articulation of the discourse in favour and against fracking technology and its underlying values as manifested in the Spanish traditional mass media and emerging social media such as Youtube. Results show that Spanish public discourse on fracking technology includes the costs-benefits analysis to communicate how natural resources from local communities may be affected by these facilities due to environmental, health and economic consequences. Furthermore, this technology is represented as a solution to the "demand of energy" according to the optimistic discourse while, from a pessimistic view, fracking is often framed as a source "environmental problems" and even natural disasters as possible earthquakes. In this latter case, this negative representation could have been influenced by the closure of a macro project to store injected natural gas in the Mediterranean Sea using the old facilities of an oil exploitation in Amposta (Proyecto Cástor). The closure of this project was due to the occurrence of earthquakes whose intensity was higher than the originally expected by the experts in the assessment stage of the project.

Síntese, caracterização e modificação de superfícies de sílicas mesoporosas ordenadas para captura de CO2

Processos como a purificação do metano (CH4) e a produção de hidrogênio gasoso (H2) envolvem etapas de separação de CO2. Atualmente, etanolaminas como monoetanolamina (MEA), dietanolamina (DEA), metildietanolamina (MDEA) e trietanolamina (TEA) são as substâncias mais utilizadas no processo de separação/captura de CO2 em processos industriais. Entretanto, o uso destas substâncias apresenta alguns inconvenientes devido à alta volatilidade, dificuldade de se trabalhar com material líquido, também ao alto gasto energético envolvido das etapas de regeneração e à baixa estabilidade térmica e química. Com base nessa problemática, esse trabalho teve por objetivo a síntese de um tipo de sílica mesoporosa altamente ordenada (SBA-15) de modo a utilizá-la no processo de captura de CO2. O trabalho foi dividido em quatro etapas experimentais que envolveram a síntese da SBA-15, o estudo do comportamento térmico de algumas etanolaminas livres, síntese e caracterização de materiais adsorventes preparados a partir de incorporação de etanolaminas à SBA-15 e estudo da eficiência de captura de CO2 por esses materiais. Novas alternativas de síntese da SBA-15 foram estudadas neste trabalho, visando aperfeiçoar as propriedades texturais do material produzido. Tais alternativas são baseadas na remoção do surfatante, utilizado como molde na síntese da sílica mesoporosa, por meio da extração por Soxhlet, utilizando diferentes solventes. O processo contribuiu para melhorar as propriedades do material obtido, evitando o encolhimento da estrutura que pode ser ocasionado durante a etapa de calcinação. Por meio de técnicas como TG/DTG, DSC, FTIR e Análise Elementar de C, H e N foi realizada a caracterização físico-química e termoanalítica da MEA, DEA, MDEA e TEA, visando melhor conhecer as características destas substâncias. Estudos cinéticos baseados nos métodos termogravimétricos isotérmicos e não isotérmicos (Método de Ozawa) foram realizados, permitindo a determinação de parâmetros cinéticos envolvidos nas etapas de volatilização/decomposição térmica das etanolaminas. Além das técnicas acima mencionadas, MEV, MET, SAXS e Medidas de Adsorção de N2 foram utilizadas na caraterização da SBA-15 antes e após a incorporação das etanolaminas. Dentre as etanolaminas estudadas, a TEA apresentou maior estabilidade térmica, entretanto, devido ao seu maior impedimento estérico, é a etanolamina que apresenta menor afinidade com o CO2. Diferentemente das demais etanolaminas estudadas, a decomposição térmica da DEA envolve uma reação intramolecular, levando a formação de MEA e óxido de etileno. A incorporação destes materiais à SBA-15 aumentou a estabilidade térmica das etanolaminas, uma vez que parte do material permanece dentro dos poros da sílica. Os ensaios de adsorção de CO2 mostraram que a incorporação da MEA à SBA-15 catalisou o processo de decomposição térmica da mesma. A MDEA foi a etanolamina que apresentou maior poder de captura de CO2 e sua estabilidade térmica foi consideravelmente aumentada quando a mesma foi incorporada à SBA-15, aumentando também seu potencial de captura de CO2.

Procedimento de avaliação de integridade estrutural de juntas soldadas circunferenciais em tubulações submarinas rígidas submetidas à flexão.

A demanda crescente por energia tem motivado a procura por petróleo e gás natural em ambientes com condições extremas, como operações em águas profundas e o transporte de fluídos corrosivos. Avanços tecnológicos recentes favorecem o uso de tubos de aço contendo uma camada interna resistente a corrosão (comumente chamados de Lined ou Clad Pipes) para o transporte de tais fluidos agressivos. Além disso, as tubulações submarinas são sujeitas a condições de instalação muito severas e, um caso de interesse, é o procedimento de reeling que permite com que a fabricação e inspeção da tubulação seja feita em terra. Apesar de possuir vantagens econômicas, a avaliação da integridade estrutural e especificação dos tamanhos toleráveis de trinca em juntas soldadas, nestas condições, torna-se uma tarefa complexa, devido a natureza dissimilar dos materiais e ao grande nível de deformação plástica no processo. Dessa maneira, este trabalho tem por objetivo o desenvolvimento de um procedimento de avaliação de forças motrizes elasto-plásticas em tubos contendo juntas soldadas circunferenciais sujeitos a flexão, para uma extensa gama de configurações geométricas. Dois métodos distintos foram desenvolvidos e analisados: a metodologia EPRI e o procedimento que utiliza a curva de tensão vs. deformação equivalente. As análises numéricas 3D fornecem os parâmetros de fratura necessários para a resolução do problema e a acurácia dos procedimentos é verificada a partir de estudos de casos e análises paramétricas.

Reconciliação de dados de uma malha de gasodutos.

O trabalho aborda a aplicação da técnica de reconciliação de dados para o balanço da movimentação de gás natural em uma malha de escoamento de gás não processado, elaborando também um método de cálculo rápido de inventário de um duto. Foram aplicadas, separadamente, a reconciliação volumétrica à condição padrão de medição e a reconciliação mássica, bem como realizadas comparações dos resultados em relação ao balanço original e verificação do balanço resultante de energia em termos de poder calorífico superior. Dois conjuntos de pesos foram aplicados, um arbitrado de acordo com o conhecimento prévio da qualidade do sistema de medição de cada um dos pontos, outro baseado no inverso da variância dos volumes diários apurados no período. Ambos apresentaram bons resultados e o segundo foi considerado o mais apropriado. Por meio de uma abordagem termodinâmica, foi avaliado o potencial impacto, ao balanço, da condensação de parte da fase gás ao longo do escoamento e a injeção de um condensado de gás natural não estabilizado por uma das fontes. Ambos tendem a impactar o balanço, sendo o resultado esperado um menor volume, massa e energia de fase gás na saída. Outros fatores de considerável impacto na qualidade dos dados e no resultado final da reconciliação são a qualidade da medição de saída do sistema e a representatividade da composição do gás neste ponto. O inventário é calculado a partir de uma regressão que se baseia em um regime permanente de escoamento, o que pode apresentar maior desvio quando fortes transientes estão ocorrendo no último dia do mês, porém a variação de inventário ao longo do mês possui baixo impacto no balanço. Concluiu-se que a reconciliação volumétrica é a mais apropriada para este sistema, pois os dados reconciliados levam os balanços mássicos e de energia em termos de poder calorífico, ambos na fase gás, para dentro do perfil esperado de comportamento. Embora um balanço volumétrico nulo apenas da fase gás não seja por si só o comportamento esperado quando se considera os efeitos descritos, para desenvolver um balanço mais robusto é necessário considerar as frações líquidas presentes no sistema, agregando maior dificuldade na aquisição e qualidade dos dados.

Resistência à fadiga de tubo API 5L X65 cladeado e soldado circunferencialmente com eletrodos de Inconel® 625

As recentes descobertas de petróleo e gás na camada do Pré-sal representam um enorme potencial exploratório no Brasil, entretanto, os desafios tecnológicos para a exploração desses recursos minerais são imensos e, consequentemente, têm motivado o desenvolvimento de estudos voltados a métodos e materiais eficientes para suas produções. Os tubos condutores de petróleo e gás são denominados de elevadores catenários ou do inglês \"risers\", e são elementos que necessariamente são soldados e possuem fundamental importância nessa cadeia produtiva, pois transportam petróleo e gás natural do fundo do mar à plataforma, estando sujeitos a carregamentos dinâmicos (fadiga) durante sua operação. Adicionalmente, um dos problemas centrais à produção de óleo e gás das reservas do Pré-Sal está diretamente associado a meios altamente corrosivos, tais como H2S e CO2. Uma forma mais barata de proteção dos tubos é a aplicação de uma camada de um material metálico resistente à corrosão na parte interna desses tubos (clad). Assim, a união entre esses tubos para formação dos \"risers\" deve ser realizada pelo emprego de soldas circunferenciais de ligas igualmente resistentes à corrosão. Nesse contexto, como os elementos soldados são considerados possuir defeitos do tipo trinca, para a garantia de sua integridade estrutural quando submetidos a carregamentos cíclicos, é necessário o conhecimento das taxas de propagação de trinca por fadiga da solda circunferencial. Assim, neste trabalho, foram realizados ensaios de propagação de trinca por fadiga na região da solda circunferencial de Inconel® 625 realizada em tubo de aço API 5L X65 cladeado, utilizando corpos de prova do tipo SEN(B) (Single Edge Notch Bending) com relações entre espessura e largura (B/W) iguais a 0,5, 1 e 2. O propósito central deste trabalho foi de obter a curva da taxa de propagação de trinca por fadiga (da/dN) versus a variação do fator de intensidade de tensão (ΔK) para o metal de solda por meio de ensaios normatizados, utilizando diferentes técnicas de acompanhamento e medição da trinca. A monitoração de crescimento da trinca foi feita por três técnicas: variação da flexibilidade elástica (VFE), queda de potencial elétrico (QPE) e análise de imagem (Ai). Os resultados mostraram que as diferentes relações B/W utilizadas no estudo não alteraram significantemente as taxas de propagação de trinca por fadiga, respeitado que a propagação aconteceu em condições de escoamento em pequena escala na frente da trinca. Os resultados de propagação de trinca por fadiga permitiram a obtenção das regiões I e II da curva da/dN versus ΔK para o metal de solda. O valor de ΔKlim obtido para o mesmo foi em torno de 11,8 MPa.m1/2 e os valores encontrados das constantes experimentais C e m da equação de Paris-Erdogan foram respectivamente iguais a 1,55 x10-10 [(mm/ciclo)/(MPa.m1/2)m] e 4,15. A propagação de trinca no metal de solda deu-se por deformação plástica, com a formação de estrias de fadiga.

Transmission and Transport of Energy in the Western U.S. and Canada: A Law and Policy Road Map

This collection of short essays arose from the inaugural meeting of the Idaho Symposium on Energy in the West, which was held in November, 2014. The topic for this first Symposium was Transmission and Transport of Energy in the Western U.S. and Canada: A Law and Policy Road Map. The essays in this collection provide a notable introduction to the major energy issues facing the West today. Topics include: building a resilient legal architecture for western energy production; natural gas flaring; transmission planning for wind energy; utilities and rooftop solar; special considerations for western states and the Clean Power Plan; the Clean Power Plan's implications for the western grid; siting renewable energy on public lands; and implications of utility reform in New York and Hawaii for the Northwest.

Integration of Sustainable Development Principles into a Community Park

Characteristics of six operating hot spring recreational facilities were reviewed to identify opportunities for integrating a range of sustainable design and operation approaches into a community park. Potential operating cost savings were evaluated for a conceptual landscape project, bathhouse project, and swimming pool project that reduced the use of electricity, natural gas, water, the discharge of water, and solid waste generation. The projects showed a combined cost savings of approximately $40,000 per year by adopting passive solar design, energy efficient lighting, native vegetation, water efficient fixtures, and a natural swimming pool. The greatest potential operating cost reductions were observed for cutbacks in the use of swimming pool water and reductions in natural gas needed for building and swimming pool heating.

NaOH and KOH for preparing activated carbons used in energy and environmental applications

Alkaline hydroxides, especially sodium and potassium hydroxides, are multi-million-ton per annum commodities and strong chemical bases that have large scale applications. Some of them are related with their consequent ability to degrade most materials, depending on the temperature used. As an example, these chemicals are involved in the manufacture of pulp and paper, textiles, biodiesels, soaps and detergents, acid gases removal (e.g., SO2) and others, as well as in many organic synthesis processes. Sodium and potassium hydroxides are strong and corrosive bases, but they are also very stable chemicals that can melt without decomposition, NaOH at 318ºC, and KOH at 360ºC. Hence, they can react with most materials, even with relatively inert ones such as carbon materials. Thus, at temperatures higher than 360ºC these melted hydroxides easily react with most types of carbon-containing raw materials (coals, lignocellulosic materials, pitches, etc.), as well as with most pure carbon materials (carbon fibers, carbon nanofibers and carbon nanotubes). This reaction occurs via a solid-liquid redox reaction in which both hydroxides (NaOH or KOH) are converted to the following main products: hydrogen, alkaline metals and alkaline carbonates, as a result of the carbon precursor oxidation. By controlling this reaction, and after a suitable washing process, good quality activated carbons (ACs), a classical type of porous materials, can be prepared. Such carbon activation by hydroxides, known since long time ago, continues to be under research due to the unique properties of the resulting activated carbons. They have promising high porosity developments and interesting pore size distributions. These two properties are important for new applications such as gas storage (e.g., natural gas or hydrogen), capture, storage and transport of carbon dioxide, electricity storage demands (EDLC-supercapacitors-) or pollution control. Because these applications require new and superior quality activated carbons, there is no doubt that among the different existing activating processes, the one based on the chemical reaction between the carbon precursor and the alkaline hydroxide (NaOH or KOH) gives the best activation results. The present article covers different aspects of the activation by hydroxides, including the characteristics of the resulting activated carbons and their performance in some environment-related applications. The following topics are discussed: i) variables of the preparation method, such as the nature of the hydroxide, the type of carbon precursor, the hydroxide/carbon precursor ratio, the mixing procedure of carbon precursor and hydroxide (impregnation of the precursor with a hydroxide solution or mixing both, hydroxide and carbon precursor, as solids), or the temperature and time of the reaction are discussed, analyzing their effect on the resulting porosity; ii) analysis of the main reactions occurring during the activation process, iii) comparative analysis of the porosity development obtained from different activation processes (e.g., CO2, steam, phosphoric acid and hydroxides activation); and iv) performance of the prepared activated carbon materials on a few applications, such as VOC removal, electricity and gas storages.