Titanium phosphate for Fuel Cell Proton Conduction Membranes

Environmental issues due to increases in emissions of air pollutants and greenhouse gases are driving the development of clean energy delivery technologies such as fuel cells. Low temperature Proton Exchange Membrane Fuel Cells (PEMFC) use hydrogen as a fuel and their only emission is water. While significant advances have been made in recent years, a major limitation of the current technology is the cost and materials limitations of the proton conduction membrane. The proton exchange membrane performs three critical functions in the PEMFC membrane electrode assembly (MEA): (i) conduction of protons with minimal resistance from the anode (where they are generated from hydrogen) to the cathode (where they combine with oxygen and electrons, from the external circuit or load), (ii) providing electrical insulation between the anode and cathode to prevent shorting, and (iii) providing a gas impermeable barrier to prevent mixing of the fuel (hydrogen) and oxidant. The PFSA (perfluorosulphonic acid) family of membranes is currently the best developed proton conduction membrane commercially available, but these materials are limited to operation below 100oC (typically 80oC, or lower) due to the thermochemical limitations of this polymer. For both mobile and stationary applications, fuel cell companies require more durable, cost effective membrane technologies capable of delivering enhanced performance at higher temperatures (typically 120oC, or higher. This is driving research into a wide range of novel organic and inorganic materials with the potential to be good proton conductors and form coherent membranes. There are several research efforts recently reported in the literature employing inorganic nanomaterials. These include functionalised silica phosphates [1,2], fullerene [3] titania phosphates [4], zirconium pyrophosphate [5]. This work addresses the functionalisation of titania particles with phosphoric acid. Proton conductivity measurements are given together with structural properties.

Hydrostability and Scaling Up Molecular Sieve Silica (MSS) Membranes for H2/CO Separation in Fuel Cell Systems

MSS membranes are a good candidate for CO cleanup in fuel cell fuel processing systems due to their ability to selectively permeate H2 over CO via molecular sieving. Successfully scaled up tubular membranes were stable under dry conditions to 400°C with H2 permeance as high as 2 x 10-6 mol.m-2.s^-1.Pa^-1 at 200 degrees C and H2/CO selectivity up to 6.4, indicating molecular sieving was the dominant mechanism. A novel carbonised template molecular sieve silica (CTMSS) technology gave the scaled up membranes resilience in hydrothermal conditions up to 400 degrees C in 34% steam and synthetic reformate, which is required for use in fuel cell CO cleanup systems.

Application of multivariate statistical process control to fuel cell manufacturing

Univariate statistical control charts, such as the Shewhart chart, do not satisfy the requirements for process monitoring on a high volume automated fuel cell manufacturing line. This is because of the number of variables that require monitoring. The risk of elevated false alarms, due to the nature of the process being high volume, can present problems if univariate methods are used. Multivariate statistical methods are discussed as an alternative for process monitoring and control. The research presented is conducted on a manufacturing line which evaluates the performance of a fuel cell. It has three stages of production assembly that contribute to the final end product performance. The product performance is assessed by power and energy measurements, taken at various time points throughout the discharge testing of the fuel cell. The literature review performed on these multivariate techniques are evaluated using individual and batch observations. Modern techniques using multivariate control charts on Hotellings T2 are compared to other multivariate methods, such as Principal Components Analysis (PCA). The latter, PCA, was identified as the most suitable method. Control charts such as, scores, T2 and DModX charts, are constructed from the PCA model. Diagnostic procedures, using Contribution plots, for out of control points that are detected using these control charts, are also discussed. These plots enable the investigator to perform root cause analysis. Multivariate batch techniques are compared to individual observations typically seen on continuous processes. Recommendations, for the introduction of multivariate techniques that would be appropriate for most high volume processes, are also covered.

Experimental and model-based analysis of the steady-state and dynamic operating behaviour of the direct methanol fuel cell (DMFC)

Direct methanol fuel cell, DMFC, model, mass transport, Maxwell-Stefan, Flory-Huggins, crossover, polymer electrolyte membrane, Nafion

Modelling of a symmetric molten carbonate fuel cell stack

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2011

Non-linear model reduction and control of molten carbonate fuel cell systems with internal reforming fuel cell systems with internal reforming

Magdeburg, Univ., Diss, 2007

Development of a glucose-oxygen enzymatic fuel cell

Magdeburg, Univ., Fak. für Verfahrens- und Systemtechnik, Diss., 2012

Análisis del ciclo de vida de sistemas de tratamiento de aguas residuales: influencia de los materiales utilizados

En este proyecto se tiene como objetivo comparar una EDAR específica con otras tres, desde el punto de vista ambiental, y establecer diferentes alternativas. En particular, se ha evaluado la mejor alternativa en la obtención de energía eléctrica para la propia utilización de la planta de tratamiento de aguas residuales, a partir del biogás generado en el digestor en la línea de lodos. En este tipo de instalaciones, entre las alternativas tanto en su uso actual como en fase de desarrollo, el motor de cogeneración de electricidad y el calor es el más utilizado para obtener simultáneamente la electricidad necesaria para las instalaciones y el calor necesario para mantener el digestor de lodos a la temperatura de trabajo (36ºC aproximadamente). Las otras alternativas evaluadas en este estudio son las pilas de biogás de membrana electrolítica polimérica (en inglés Polymeric Electrolyte Membrane, PEM) y las pilas de óxidos sólidos (en inglés Solid Oxide Fuel Cells, SOFC) con una turbina de gas (sistema híbrido SOFC-GT). Por otro lado, se estudian las características de los materiales que componen los dispositivos MEC (microbial electrolysis cell) y las pilas PEM y SOFC, así como las ventajas e inconvenientes de usar estas nuevas tecnologías en el tratamiento de aguas residuales, así como la evaluación del impacto ambiental de la EDAR objeto de estudio, que se ha llevado a cabo utilizando el análisis de ciclo de vida (ACV). El ACV es una herramienta que permite comparar diferentes procesos o productos que tengan la misma función, y así evaluar la alternativa que conlleve una mejora en el medio ambiental. La metodología de ACV pretende evaluar en detalle el ciclo de vida completo de un producto o proceso. Un ACV se suele definir de tipo "cradle to grave" o "desde la cuna hasta la tumba" o bien de tipo "gate to gate", o "de puerta a puerta". En el primer caso el estudio analiza el ciclo de vida completo del sistema, dese el origen hasta el final, mientras que en el segundo caso el ACV no tiene en cuenta su disposición final (vertedero, reciclaje, etc.). Un estudio de ACV del primer tipo conlleva hacer un estudio muy detallado, que en la práctica puede resultar muy largo y laborioso por la dificultad de encontrar todos los datos necesarios. Por ello, muchos estudios de ACV que se encuentran en la literatura suelen ser del tipo "gate to gate". Además, hay que esablecer las fronteras del sistema a estudiar, ya que hay procesos que tienen muy poca contribución a las categorías de impacto ambiental. En una EDAR los principales procesos considerados en el ACV llevado a cabo son el consumo de productos químicos, de electricidad, la producción de lodos y su utilización como composta, el biogás y su utilización para producir electricidad, los residuos sólidos y las distintas emisiones al medio producidas por el propio funcionamiento de la EDAR. Las operaciones relacionadas indirectamente como el transporte de los lodos, de productos químicos, de los residuos sólidos y la infraestructura con una vida media de 30 años no influyen significativamente en los resultados, por ejemplo el transporte de los lodos con un camión a 30km contribuyen en menos de 1% en todas las categorías de impacto. De acuerdo con las normativas ISO series 14040 que regulan las pautas de un ACV, se establece una unidad funcional apropiada, o sea habitante equivalente, ya que es la más apropiada por tener en cuenta la carga contaminante en el agua a tratar, parámetro imprescindible para comparar EDARs. Redefiniendo las fronteras, se realiza un ACV del depósito del biogás sin tener en cuenta el resto de la instalación y se toma como unidad funcional m3 de biogás, en el caso concreto de obtener biogás mediante un dispositivo MEC, que maximiza la cantidad de hidrógeno en detrimento de la cantidad de metano contenido en el biogás, observándose que la contribución de un biogás con un alto contenido en hidrógeno y, por tanto bajo en metano, produce una mejora ambiental. Las categorías de impacto ambiental que tienen contribución son el calentamiento global y la oxidación fotoquímica; el dispositivo MEC hace quela contribución a estas categorías de impacto sea de un orden de magnitud inferior con respecto al biogás generado en un digestor. Además, si se produce la combustión del biogás, la única categoría de impacto que tiene contribución es la de calentamiento global; para una dispositivo MEC la contribución sigue siendo un orden de magnitud inferior con respecto al biogás de un digestor de lodos.

Pilhas a combustível de óxido sólido: materiais, componentes e configurações

In this paper the current status of fuel cells is described with particular emphasis on high (T > 800 ºC) and intermediate (T < 800 ºC) temperature solid oxide fuel cells. Also the importance of the fuel cell technology is shown. Reviewed are the fundamental features, the basic principles, types of fuel cell, fabrication methods, cell configurations and the development of components (cathodes, anodes, electrolytes, interconnect) and materials.

A utilização de etanol em célula a combustível de óxido sólido

This work reports a review on the status and technical feasibility of the application of ethanol as fuel for Solid Oxide Fuel Cells (SOFC), presenting both external reform and cell with direct utilization of ethanol. Based on this survey, both experimental results and mathematical modeling indicated the technical feasibility of power generation by ethanol SOFC, with cell units producing 450 mW/cm², sufficient for scale up to large stationary plants. The quantitative assessments in the literature show this field to be promising for researchers and private sector investment as well being a strategic technology for government policy in the short and long term.

Tasajännitetason nosto polttokennosovelluksessa

Polttokennojen, erityisesti SOFC-kennojen, tutkimuksessa on viime vuosina saavutettu merkittäviä edistysaskelia ja mahdollisuudet kennojen laajamittaiseen hyödyntämiseen paranevat koko ajan. Polttokennojen yleistyessä tarvitaan tehoelektroniikkaa muokkaamaan kennojen tasajännite verkkoon sopivaksi vaihtojännitteeksi. Verkkovaihtosuuntaaja vaatii korkeamman jännitetason, kuin polttokennosta on saatavissa, joten tasajännitetasoa on ensin nostettava. Tässä diplomityössä esitellään kolme eri hakkuritopologiaa ja perehdytään kokosiltahakkurin optimointiin. Hakkurin pääasialliset häviölähteet olivat toision diodisilta ja transistorit. Diodien vaihtaminen piidiodeista piikarbididiodeihin ei parantanut hyötysuhdetta, koska toision jännite tarkastellussa sovelluksessa oli matala. Muuntajan käämiminen litz-johtimella paransi hyötysuhdetta merkittävästi.

Effect of Material Recycling on the Feasibility of Solid Recovered Fuel Fired Power Plant

This master’s thesis examines the effects of increased material recycling on different waste-to-energy concepts. With background study and a developed techno-economic computational method the feasibility of chosen scenarios with different combinations of mechanical treatment and waste firing technologies can be evaluated. The background study covers the waste scene of Finland, and potential market areas Poland and France. Calculated cases concentrate on municipal solid waste treatment in the Finnish operational environment. The chosen methodology to approach the objectives is techno-economic feasibility assessment. It combines calculation methods of literature and practical engineering to define the material and energy balances in chosen scenarios. The calculation results together with other operational and financial data can be concluded to net present values compared between the scenarios. For the comparison, four scenarios, most vital and alternative between each other, are established. The baseline scenario is grate firing of source separated mixed municipal solid waste. Second scenario is fluidized bed combustion of solid recovered fuel produced in mechanical treatment process with metal separation. Third scenario combines a biomaterial separation process to the solid recovered fuels preparation and in the last scenario plastics are separated in addition to the previous operations. The results indicated that the mechanical treatment scenarios still need to overcome some problems to become feasible. Problems are related to profitability, residue disposal and technical reliability. Many uncertainties are also related to the data gathered over waste characteristics, technical performance and markets. With legislative support and development of further processing technologies and markets of the recycled materials the scenarios with biomaterial and plastic separation may operate feasibly in the future.

Modelling and simulation of a photovoltaic fuel cell hybrid system

A stand-alone power system is an autonomous system that supplies electricity to the user load without being connected to the electric grid. This kind of decentralized system is frequently located in remote and inaccessible areas. It is essential for about one third of the world population which are living in developed or isolated regions and have no access to an electricity utility grid. The most people live in remote and rural areas, with low population density, lacking even the basic infrastructure. The utility grid extension to these locations is not a cost effective option and sometimes technically not feasible. The purpose of this thesis is the modelling and simulation of a stand-alone hybrid power system, referred to as “hydrogen Photovoltaic-Fuel Cell (PVFC) hybrid system”. It couples a photovoltaic generator (PV), an alkaline water electrolyser, a storage gas tank, a proton exchange membrane fuel cell (PEMFC), and power conditioning units (PCU) to give different system topologies. The system is intended to be an environmentally friendly solution since it tries maximising the use of a renewable energy source. Electricity is produced by a PV generator to meet the requirements of a user load. Whenever there is enough solar radiation, the user load can be powered totally by the PV electricity. During periods of low solar radiation, auxiliary electricity is required. An alkaline high pressure water electrolyser is powered by the excess energy from the PV generator to produce hydrogen and oxygen at a pressure of maximum 30bar. Gases are stored without compression for short- (hourly or daily) and long- (seasonal) term. A proton exchange membrane (PEM) fuel cell is used to keep the system’s reliability at the same level as for the conventional system while decreasing the environmental impact of the whole system. The PEM fuel cell consumes gases which are produced by an electrolyser to meet the user load demand when the PV generator energy is deficient, so that it works as an auxiliary generator. Power conditioning units are appropriate for the conversion and dispatch the energy between the components of the system. No batteries are used in this system since they represent the weakest when used in PV systems due to their need for sophisticated control and their short lifetime. The model library, ISET Alternative Power Library (ISET-APL), is designed by the Institute of Solar Energy supply Technology (ISET) and used for the simulation of the hybrid system. The physical, analytical and/or empirical equations of each component are programmed and implemented separately in this library for the simulation software program Simplorer by C++ language. The model parameters are derived from manufacturer’s performance data sheets or measurements obtained from literature. The identification and validation of the major hydrogen PVFC hybrid system component models are evaluated according to the measured data of the components, from the manufacturer’s data sheet or from actual system operation. Then, the overall system is simulated, at intervals of one hour each, by using solar radiation as the primary energy input and hydrogen as energy storage for one year operation. A comparison between different topologies, such as DC or AC coupled systems, is carried out on the basis of energy point of view at two locations with different geographical latitudes, in Kassel/Germany (Europe) and in Cairo/Egypt (North Africa). The main conclusion in this work is that the simulation method of the system study under different conditions could successfully be used to give good visualization and comparison between those topologies for the overall performance of the system. The operational performance of the system is not only depending on component efficiency but also on system design and consumption behaviour. The worst case of this system is the low efficiency of the storage subsystem made of the electrolyser, the gas storage tank, and the fuel cell as it is around 25-34% at Cairo and 29-37% at Kassel. Therefore, the research for this system should be concentrated in the subsystem components development especially the fuel cell.